CN108772614A - A kind of residents in rural community processing equipment with oxygen dispersion mouth - Google Patents
A kind of residents in rural community processing equipment with oxygen dispersion mouth Download PDFInfo
- Publication number
- CN108772614A CN108772614A CN201810496113.3A CN201810496113A CN108772614A CN 108772614 A CN108772614 A CN 108772614A CN 201810496113 A CN201810496113 A CN 201810496113A CN 108772614 A CN108772614 A CN 108772614A
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- axis
- oxygen
- sliding
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- mounting bracket
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-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B23—MACHINE TOOLS; METAL-WORKING NOT OTHERWISE PROVIDED FOR
- B23K—SOLDERING OR UNSOLDERING; WELDING; CLADDING OR PLATING BY SOLDERING OR WELDING; CUTTING BY APPLYING HEAT LOCALLY, e.g. FLAME CUTTING; WORKING BY LASER BEAM
- B23K7/00—Cutting, scarfing, or desurfacing by applying flames
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B23—MACHINE TOOLS; METAL-WORKING NOT OTHERWISE PROVIDED FOR
- B23K—SOLDERING OR UNSOLDERING; WELDING; CLADDING OR PLATING BY SOLDERING OR WELDING; CUTTING BY APPLYING HEAT LOCALLY, e.g. FLAME CUTTING; WORKING BY LASER BEAM
- B23K37/00—Auxiliary devices or processes, not specially adapted to a procedure covered by only one of the preceding main groups
- B23K37/02—Carriages for supporting the welding or cutting element
- B23K37/0252—Steering means
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B23—MACHINE TOOLS; METAL-WORKING NOT OTHERWISE PROVIDED FOR
- B23K—SOLDERING OR UNSOLDERING; WELDING; CLADDING OR PLATING BY SOLDERING OR WELDING; CUTTING BY APPLYING HEAT LOCALLY, e.g. FLAME CUTTING; WORKING BY LASER BEAM
- B23K7/00—Cutting, scarfing, or desurfacing by applying flames
- B23K7/10—Auxiliary devices, e.g. for guiding or supporting the torch
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L75/00—Compositions of polyureas or polyurethanes; Compositions of derivatives of such polymers
- C08L75/04—Polyurethanes
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23D—BURNERS
- F23D14/00—Burners for combustion of a gas, e.g. of a gas stored under pressure as a liquid
- F23D14/38—Torches, e.g. for brazing or heating
- F23D14/42—Torches, e.g. for brazing or heating for cutting
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23D—BURNERS
- F23D14/00—Burners for combustion of a gas, e.g. of a gas stored under pressure as a liquid
- F23D14/46—Details, e.g. noise reduction means
- F23D14/465—Details, e.g. noise reduction means for torches
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23D—BURNERS
- F23D14/00—Burners for combustion of a gas, e.g. of a gas stored under pressure as a liquid
- F23D14/46—Details, e.g. noise reduction means
- F23D14/48—Nozzles
- F23D14/52—Nozzles for torches; for blow-pipes
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23D—BURNERS
- F23D14/00—Burners for combustion of a gas, e.g. of a gas stored under pressure as a liquid
- F23D14/46—Details, e.g. noise reduction means
- F23D14/62—Mixing devices; Mixing tubes
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23D—BURNERS
- F23D14/00—Burners for combustion of a gas, e.g. of a gas stored under pressure as a liquid
- F23D14/46—Details, e.g. noise reduction means
- F23D14/66—Preheating the combustion air or gas
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K2201/00—Specific properties of additives
- C08K2201/002—Physical properties
- C08K2201/003—Additives being defined by their diameter
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K2201/00—Specific properties of additives
- C08K2201/011—Nanostructured additives
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L2205/00—Polymer mixtures characterised by other features
- C08L2205/03—Polymer mixtures characterised by other features containing three or more polymers in a blend
- C08L2205/035—Polymer mixtures characterised by other features containing three or more polymers in a blend containing four or more polymers in a blend
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23D—BURNERS
- F23D2900/00—Special features of, or arrangements for burners using fluid fuels or solid fuels suspended in a carrier gas
- F23D2900/21—Burners specially adapted for a particular use
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/34—Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- General Engineering & Computer Science (AREA)
- Optics & Photonics (AREA)
- Physics & Mathematics (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Processing Of Solid Wastes (AREA)
- Heat Treatment Of Articles (AREA)
Abstract
A kind of residents in rural community processing equipment with oxygen dispersion mouth, workbench fix the upper end that branch is located at supporting rack, and workbench is mainly made of several grids;Reject chute is slidably disposed within the lower section of workbench by a pair of of sliding slot;Side is equipped with the balladeur train slided along its length on the table, and two vertical beam lower ends of balladeur train are arranged the slideway on table surface with left and right directions by two X-axis sliding equipments and are slidably matched;Z-axis lifting mechanism is coordinated by the crossbeam of Y-axis sliding equipment and balladeur train in front-rear direction;The screw rod rotation that the driving of Z axis servo motor is vertically arranged in Z-axis lifting mechanism, cutting nozzle is connect with screw rod by screw-thread fit sliding pair;Servo motor in X-axis sliding equipment, Y-axis sliding equipment and Z-axis lifting mechanism is connect with controller;There is the mixer that can mix acetylene and oxygen in cutting nozzle, and disperse mouth with oxygen to improve the dispersion degree of oxygen.The device is easy to implement the quick adjustment of cutting torch mouth position, and its good cutting effect.
Description
Technical field
The invention belongs to environmentally friendly house refuse block drying and other treatment fields, and in particular to a kind of rural area with oxygen dispersion mouth
Domestic garbage treatment equipment.
Background technology
House refuse block processing cutter device coordinates different working gas that can cut the cutting of various oxygen to be difficult to cut
House refuse block, such as iron refuse object, stainless steel rubbish object or other nonflammable rubbish blocks.Currently, market
Laser cutting is opened or used to upper house refuse block cutter device generally using manual, using processing by hand firstly the need of making one
With arched door shape template, cut afterwards along first perforating.This mode speed is slow, and effect is poor, and has certain danger, at
This is also higher.
In addition, traditional house refuse block processing cutter device flexibility is poor, it is not easy to the position adjustment of cutting nozzle, is cut
It cuts less efficient;In addition, in traditional house refuse block cutter device mixed gas mix it is uneven, cutting temperature is relatively low,
Limit its operating efficiency.
Invention content
In view of the above existing problems in the prior art, the present invention provides a kind of residents in rural community disperseing mouth with oxygen
Processing equipment, device flexibility is good for this, is easy to implement the quick adjustment of cutting torch mouth position, and the uniformity of its internal mix gas
Height, good cutting effect, cutting efficiency is high, which does not need human hand and directly operate, and can effectively reduce the generation of production accident.
To achieve the goals above, the present invention also provides a kind of residents in rural community processing disperseing mouth with oxygen to set
It is standby, including supporting rack, workbench, cutting nozzle, reject chute, Y-axis sliding equipment, cooler and controller, the workbench fix
Branch is located at the upper end of supporting rack, and workbench is made of the connecting rod between several equally distributed grids and connection adjacent cells;
A pair of of sliding slot that left and right extends is provided with below workbench, a pair of of sliding slot is respectively fixedly connected on the inside of supporting rack
Front-end and back-end;The reject chute is slidably arranged in the lower section of workbench by coordinating with a pair of of sliding slot;On the table
Side is provided with the balladeur train slided along its length, and the balladeur train is by horizontal crossbeam and is fixedly connected on crossbeam both ends lower part
Vertical beam forms;Two horizontal slideways are provided on the outside of two vertical beams, two slideways are respectively fixedly connected on the table
The front-end and back-end in portion, the slideway are made of the X-axis sliding rail positioned inside and the X-axis balladeur train item positioned at outside;
Two X-axis sliding equipments being slidably matched respectively with two slideways are respectively fixedly connected in the outside of two vertical beam lower ends;The X
Axis sliding equipment includes X-axis gear mounting bracket, X-axis movement sliding block, X-axis balladeur train and X-axis servo motor, the X-axis gear
It is fixedly connected by the link above slideway between mounting bracket and vertical beam, the X-axis movement sliding block is mounted on link
Inside, and be slidably matched with X-axis sliding rail;Upper and lower part in X-axis gear mounting bracket is rotationally equipped with X respectively
Axis driving gear and X-axis driven gear, pass through synchronous tooth profile band connection between X-axis driving gear and X-axis driven gear;The X
Axis balladeur train and X-axis driven gear are co-axially mounted on the lower part on the inside of X-axis gear mounting bracket, and with X-axis balladeur train item
Engagement;The X-axis servo motor is mounted on the upper outside of X-axis gear mounting bracket, and is drivingly connected with X-axis driving gear;
The cooler includes cooling shell, the cooling enclosure interior by be separately positioned on two of upper and lower part every
Plate is divided into three parts, respectively two buffered rooms positioned at the heat-exchanging chamber at middle part and below and above;It is described
The upper, middle and lower of heat-exchanging chamber be respectively arranged be connected to its inner cavity by coolant liquid outlet, medicament inlet and by
Coolant inlet, the interior central area of heat-exchanging chamber are fixedly installed more heat-exchange tubes, the upper end of more heat-exchange tubes and
Lower end respectively penetrates two buffered rooms below and above;Two buffered rooms of upper and lower part are respectively set
There are the refrigerant inlet being connected to its inner cavity and refrigerant exit;Cooler is fixed at outside the X-axis electric machine casing of X-axis servo motor
Portion, the X-axis electric machine casing is the hollow structure with inner cavity, and X-axis electric machine casing is connected with the feed liquor being connected to its inner cavity
Pipeline and outlet tube road;The inlet pipe is connected with by coolant liquid outlet, and the input end of the outlet tube road and water pump connects,
The outlet end of water pump is connect with by coolant liquid entrance;
It has been respectively fixedly connected with horizontally disposed Y-axis sliding rail at left and right sides of the crossbeam and has stated Y-axis balladeur train
Item;It is slidably provided with Y-axis sliding equipment on the top of crossbeam;The Y-axis sliding equipment includes Y-axis gear mounting bracket, Y-axis shifting
Movable slider, Y-axis balladeur train and Y-axis servo motor;The Y-axis movement sliding block and Y-axis gear mounting bracket are respectively distributed to crossbeam
Left and right sides difference, and be fixedly connected with Y-axis gear mounting bracket by connecting plate;The Y-axis movement sliding block slides rail with Y-axis
Road is slidably matched;It is rotationally equipped with Y-axis driving gear and Y-axis driven gear, Y-axis respectively in the Y-axis gear mounting bracket
Pass through synchronous tooth profile band connection between driven gear and Y-axis driving gear;The Y-axis balladeur train and Y-axis driven gear are coaxial
Ground is mounted on the inside of Y-axis gear mounting bracket, and is engaged with Y-axis balladeur train item;The Y-axis servo motor is mounted on Y-axis tooth
The outside of mounting bracket is taken turns, and is drivingly connected with Y-axis driving gear;
The cutting nozzle is set to the left side of Z-axis lifting mechanism, and the Z-axis lifting mechanism includes Z axis mounting bracket, screw rod, Z
Axis servo motor and sliding pair;The Z axis mounting bracket by top plate and bottom plate, connection top plate and bottom plate between left end side end panel and
It is connected to the postive stop baffle composition of side end panel rear and front end;The screw rod is rotatably connected between top plate and bottom plate;The Z axis is watched
Take motor and be fixed at top plate top, and its output shaft penetrate rotatably top plate after connect with the upper end of screw rod;The cunning
Dynamic pair is slideably positioned between two postive stop baffles, and its center offers threaded hole;Sliding pair is set in by screw-thread fit
The outside of screw rod;The strip-shaped hole being longitudinally extended is provided in the middle part of side end panel;Pass through sliding between the cutting nozzle and sliding pair
Connecting rod across strip-shaped hole is fixedly connected;Two postive stop baffles are fixedly connected away from the side of side end panel with Y-axis movement sliding block;Institute
Cutting nozzle is stated to include cutting nozzle shell and the mixing chamber in cutting nozzle enclosure interior center, the surrounding of the cutting nozzle shell is arranged
It is provided with a large amount of through-holes;There is flame jet, the inner part of cutting nozzle shell to be sprayed close to flame for the lower end of the cutting nozzle shell
The position of mouth is fixedly installed igniter;One end of acetylene hose penetrated by cutting nozzle case top and with the upper open end of mixing chamber
Connection, the other end of acetylene hose are connect with positioned at external acetylene source of supply;One end of oxygen hose penetrates in acetylene hose and in end
Portion is fixedly connected with oxygen dispersion mouth, and the other end of oxygen hose is connect with positioned at external oxygen supply source;Cutting temperature senses
Device is fixed on the outside of flame jet;The oxygen dispersion mouth includes oxygen dispersion mouth shell, and the oxygen disperses mouth shell
Upper end, lower end be respectively arranged with oxygen inlet, oxygen dispersion mouth;Disperse mouth enclosure interior shaft core position from top to bottom in oxygen
It is disposed with oxygen and accelerates rotation cardan shaft, speedup fan room, oxygen accelerating chamber, surge chamber and oxygen spray pipe;Speedup wind
Fan the tubular structure that room, oxygen accelerating chamber, surge chamber and oxygen spray pipe are upper and lower opening, and the company by being radially arranged
The madial wall that bar disperses mouth shell with oxygen is fixedly connected;Accelerate the upper end of rotation cardan shaft and is fixed at oxygen dispersion mouth
The propulsion driving motor output shaft of shell upper end center connects, accelerate the lower end of rotation cardan shaft stretch into speedup fan room and with
Speedup fan is drivingly connected;The upper end of oxygen accelerating chamber is fixedly connected with the lower end of speedup fan room, oxygen accelerating chamber and buffering
The upper end of room connects, and the lower end of surge chamber is fixedly connected with the upper end of oxygen spray pipe;The internal diameter of oxygen spray pipe is less than buffering
The internal diameter of room;The junction of oxygen accelerating chamber and surge chamber is provided with air door, is arranged in external air damper controller and air door
Control connection;It is internally provided with wind speed inductor in surge chamber;The surface of oxygen spray pipe is provided with a large amount of through-holes;Disperse in oxygen
The upper end of mouth shell is provided with multiple acetylene flow-disturbings hole;
The igniter promotes driving motor, air damper controller, wind speed inductor, cutting temperature sensor, X-axis servo
Motor, Y-axis servo motor, Z axis servo motor and water pump are connect with controller.
In the technical scheme, the movement on left and right directions can be realized by X-axis sliding equipment, pass through Y-axis sliding equipment
It can realize the movement on front-rear direction, the movement in upper and lower directions can be realized by Z axis sliding equipment, so as to make cutting nozzle exist
It is easily moved on three degree of freedom, can make cutting nozzle that there is good moving range, with to being placed on table surface
House refuse block on different location is easily cut.The device flexibility is good, convenient for adjusting the position of cutting nozzle, can realize
Fly-cutting to house refuse block, and cut quality can be effectively ensured.Workbench is by several equally distributed grids and company
The connecting rod composition between adjacent cells is connect, the small block or powdered object that cutting can be convenient for generate fall, and are being worked by being arranged
The reject chute of platform lower part receives, in order to collect.By the setting of cooler, can be convenient for carrying out fast prompt drop to X-axis servo motor
Temperature, so as to be conducive to extend the service life of X-axis servo motor.The setting for disperseing mouth and surge chamber by oxygen, can be convenient for
It realizes the mixing of mixed gas evenly, cutting temperature can be effectively improved, so as to improve cutting efficiency.
As a preferred embodiment, it is solid cylinder that the oxygen, which accelerates rotation cardan shaft,.
The temperature of flame when further, in order to improve cutting further includes acetylene to improve cutting speed and cut quality
Pipe, oxygen hose and cutting temperature sensor, the cutting nozzle include cutting nozzle shell and setting in cutting nozzle enclosure interior center
Mixing chamber, the surrounding of the cutting nozzle shell is provided with a large amount of through-holes;
The lower end of the cutting nozzle shell has flame jet, and the inner part of cutting nozzle shell is close to the position of flame jet
It is fixedly installed igniter;
One end of the acetylene hose is penetrated by cutting nozzle case top and is connect with the upper open end of mixing chamber, acetylene hose
The other end is connect with positioned at external acetylene source of supply;One end of the oxygen hose penetrates in acetylene hose, the other end of oxygen hose
It is connect with positioned at external oxygen supply source;
The cutting temperature sensor is fixed on the outside of flame jet;
The igniter, cutting temperature sensor are connect with controller.It can be convenient for by cutting temperature sensor real-time
Measure the temperature of cutting flame.
Further, in order to enable the temperature higher of cutting flame, preferably to ensure cutting effect, the cutting nozzle shell
Internal portion is fixedly connected with interior cover body, and tempering channel is formed between interior cover body and cutting nozzle shell, is tempered the lower end connection in channel
Flame jet, the upper end for being tempered channel are connected by being tempered valve with entrance of the fixing sleeve loaded on the heat exchanger outside acetylene hose
It connects, the outlet of heat exchanger extends to cutting nozzle hull outside.
Further, for the ease of realizing the control of accurate cutting position, the left and right ends of the X-axis sliding rail are respectively provided with
Have and moves the matched X-axis Overstroke detector in sliding block left and right ends with X-axis;The left and right ends of the Y-axis sliding rail are equal
It is provided with and moves the matched Y-axis Overstroke detector in sliding block left and right ends with Y-axis;It is installed in the Y-axis gear mounting bracket
It is useful for the speed probe of detection Y-axis driving gear rotating speed;The opposite side of the top plate and bottom plate is mounted on and slides
The secondary matched Z axis Overstroke detector of upper and lower ends;The X-axis Overstroke detector, the detection of Y-axis Overstroke
Device, speed probe and Z axis Overstroke detector are connect with controller.
Further, in order to ensure that the temperature of cutting flame, the outer side covering of the cutting nozzle upper part of the housing have insulating layer.
Further, for the ease of adjusting the height of supporting rack, to realize that the adjustment of height of table, support frame as described above have
The bottom of four supporting legs, every supporting leg is both provided with height-adjustable adjustable angled seat.
As a preferred embodiment, support frame as described above is formed by stainless steel tube welding production, the thickness of stainless steel tube be 5cm~
8cm;The X-axis sliding rail material is nickel-clad steel plate, and thickness is 1cm~3cm;The Y-axis sliding rail material is nickel plating
Steel plate, thickness are 1cm~3cm;The distance between the reject chute and workbench are 10cm~15cm;The flame jet is in
Truncated conical shape;The mixing chamber is in coniform.
Further, in order to improve heat insulation effect, the insulating layer is made of high molecular material.
Further, in order to which the resistance to compression and resistance to deformation intensity that make oxygen spray pipe are more preferable, the oxygen spray pipe is by weight
Number is than composed of the following components:
338.7~563.8 parts of purified water, 2- methyl-pentadecanoic acid -2- ethyls -2- [[(2- methyl-1s-oxo pentadecyl)
Oxygen] methyl generation] 130.6~172.4 parts of 1,3- propylidene ester, 4- methoxyl groups-α-[[methyl sulphonyl] oxygroup] imino group]-benzene
133.8~242.9 parts of base acetonitrile, 3- (methyl mercapto) -129.8~146.3 parts of butyraldehyde, 132.1~189.2 parts of everbright red toner C, (1-
Methyl ethylidene) bis- (4,1- phenoxy group -2,1- ethylidene) 135.3~196.7 parts of diacetates, molybdenum nanoparticle 137.4~
192.3 parts, 130.0~172.0 parts of the polymer of newtrex and alpha -hydro-omega -hydroxypoly (oxidation -1,2- second diyl), formaldehyde
With 132.0~172.4 parts of the polymer of [complex compound of 4- (1,1- dimethyl ethyl) phenol and magnesia], alkali formula aluminium hydroxyacetate
132.3~155.9 parts, 121.5~157.0 parts of the polymethylene polyphenylene isocyanates of methyl ethyl ketoxime sealing end, 2- methyl is pungent
120.3~163.4 parts of aldehyde, 129.5~174.1 parts of formic acid -4- cyclo-octene -1- alcohol esters, polyurethane elastomer 139.8~183.6
Part, mass concentration is 162.5~216.4 parts of the hexadecanyl phosphate fatting agent of 129ppm~396ppm.
Further, in order to which the resistance to compression and resistance to deformation intensity that make oxygen spray pipe are more preferable, the making side of the oxygen spray pipe
Method is as follows:
S1:In energy-saving type stirred reactor, purified water and 2- methyl-pentadecanoic acid -2- ethyls -2- [[(2- methyl-is added
1- oxos pentadecyl) oxygen] methyl generation] 1,3- propylidene esters, start the blender in energy-saving type stirred reactor, setting speed
For 131rpm~177rpm;Start energy-saving type stirred reactor in steam coil heater, make temperature rise to 146.7 DEG C~
147.8 DEG C, 4- methoxyl groups-α-[[methyl sulphonyl] oxygroup] imino group is added]-phenylacetonitrile stirs evenly, organic matter is made
Ⅰ;
S2:It is 122.7m that organic matter made from S1 I, which is passed through flow,3/ min~163.3m3The xenon 123.6 of/min~
134.4 minute;The pH value for adjusting solution in energy-saving type stirred reactor is 4.1~8.2, keeps the temperature 123.1~363.1 minutes;It crosses
Filter, removal impurity, obtain suspension;
S3:Polymerizeing for formaldehyde and [complex compound of 4- (1,1- dimethyl ethyls) phenol and magnesia] is added in S2 suspension
Object, adjustment pH value form sediment purifying water elution between 1.5~2.0;Solid content is obtained by centrifuge, high temperature is dry
It is dry, 0.882 × 10 is crossed after grinding3Mesh sieves;Obtain the mixture of character change;
S4:The mixture that character made from S3 is changed adds to the methyl ethyl ketoxime that mass concentration is 133ppm~363ppm
In the polymethylene polyphenylene isocyanates of sealing end;Start the steam coil heater in energy-saving type stirred reactor, setting
Energy-saving type stirred reactor operating parameter is:Temperature is 207.8 DEG C~263.3 DEG C;PH is adjusted between 4.1~8.1;Pressure is
1.29MPa~1.3MPa;Reaction time is 0.4~0.9 hour;After reaction, it is depressurized to zero gauge pressure, is discharged into molding press,
Obtain oxygen spray pipe.
Description of the drawings
Fig. 1 is the structural schematic diagram of the present invention;
Fig. 2 is the structural schematic diagram of X-axis sliding equipment in the present invention;
Fig. 3 is the structural schematic diagram of cooler in the present invention;
Fig. 4 is the structural schematic diagram of Y-axis sliding equipment in the present invention;
The structural schematic diagram of Z-axis lifting mechanism in Fig. 5 present invention;
Fig. 6 is the structural schematic diagram of cutting nozzle in the present invention;
Fig. 7 is the structural schematic diagram of oxygen dispersion mouth in the present invention;
Fig. 8 be in the present invention partition board service life with usage time variation diagram.
In figure:1, supporting rack, 2, adjustable angled seat, 3, reject chute, 4, workbench, 5, X-axis sliding equipment, 5-1, X-axis servo
Motor, 5-2, X-axis driven gear, 5-3, X-axis driving gear, 5-4, X-axis balladeur train, 5-5, X-axis balladeur train item, 5-6, X
Axis sliding rail, 5-7, X-axis move sliding block, 5-8, link, 5-9, cooler, 5-9-1, by coolant liquid entrance, 5-9-2, heat
Pipe is exchanged, 5-9-3, heat-exchanging chamber, 5-9-4, partition board, 5-9-5, buffered room, 5-9-7,5-9-6, refrigerant inlet are cooled
Liquid exports, 5-9-8, medicament inlet, 5-9-9, refrigerant exit, 5-10, X-axis gear mounting bracket, and 6, Y-axis sliding equipment, 6-1, Y
Axis servo motor, 6-2, Y-axis driven gear, 6-3, Y-axis driving gear, 6-4, Y-axis balladeur train, 6-5, Y-axis balladeur train item,
6-6, Y-axis sliding rail, 6-7, Y-axis move sliding block, 6-8, connecting plate, 6-9, Y-axis gear mounting bracket, 7, Z-axis lifting mechanism, 7-
1, Z axis servo motor, 7-2, sliding pair, 7-3, screw rod, 7-4, top plate, 7-5, Z axis mounting bracket, 7-7,7-6, postive stop baffle are cut
Torch tip, 7-7-1, flame jet, 7-7-2, igniter, 7-7-3, mixing chamber, 7-7-4, tempering channel, 7-7-5, insulating layer, 7-
7-6, heat exchanger, 7-7-7, tempering valve, 7-7-8, oxygen hose, 7-7-9, acetylene hose, 7-7-10, cutting nozzle shell, 7-7-
11, interior cover body, 7-7-12, oxygen dispersion mouth, 7-7-12-1, acetylene flow-disturbing hole, 7-7-12-2, oxygen dispersion mouth, 7-7-12-3,
Oxygen spray pipe, 7-7-12-4, surge chamber, 7-7-12-5, oxygen accelerating chamber, 7-7-12-6, speedup fan room, 7-7-12-7,
Oxygen accelerates rotation cardan shaft, 7-7-12-8, oxygen inlet, 7-7-12-9, air damper controller, 7-7-12-10, wind speed induction
Device, 7-7-12-11, speedup fan, 7-7-12-12, air door, 7-8, side end panel, 7-9, bottom plate, 8, controller, 9, sliding slot, 10,
Crossbeam, 11, vertical beam.
Specific implementation mode
The invention will be further described below in conjunction with the accompanying drawings.
As shown in Figures 1 to 7, a kind of residents in rural community processing equipment with oxygen dispersion mouth, including supporting rack 1,
Workbench 4, cutting nozzle 7-7, reject chute 3, Y-axis sliding equipment 6, cooler 5-9 and controller 8, controller 8 are internally provided with
PLC control modules, the PLC control modules pass through data line and terminal PC machine data connection.The workbench 4 is fixed branch and is located at
The upper end of supporting rack 1 can be welded on the upper end of supporting rack 1;Workbench 4 is by several equally distributed grids and connects adjacent
Connecting rod composition between grid;
A pair of of sliding slot 9 that left and right extends is provided with below workbench 4, a pair of of sliding slot 9 is respectively fixedly connected in supporting rack 1
The front-end and back-end of inside;The reject chute 3 is slidably arranged in the lower section of workbench 4 by coordinating with a pair of of sliding slot 9;In work
Make 4 top of platform and be provided with the balladeur train slided along its length, the balladeur train is by horizontal crossbeam 10 and is fixedly connected on crossbeam
The vertical beam 10 at 10 both ends lower part forms;Two horizontal slideways are provided in the outside of two vertical beams 10, two slideways are solid respectively
Surely be connected to the front-end and back-end on 4 top of workbench, the slideway by positioned inside X-axis sliding rail 5-6 and be located at outside
X-axis balladeur train 5-5 composition;Two X-axis sliding equipments 5 being slidably matched respectively with two slideways are respectively fixedly connected with
The outside of two 10 lower ends of vertical beam;The X-axis sliding equipment 5 includes X-axis gear mounting bracket 5-10, X-axis movement sliding block 5-7, X-axis
Balladeur train 5-4 and X-axis servo motor 5-1, by being located above slideway between the X-axis gear mounting bracket 5-10 and vertical beam 10
Link 5-8 be fixedly connected, X-axis movement sliding block 5-7 is mounted on the inside of link 5-8, and with X-axis sliding rail 5-
6 are slidably matched, and specifically, the X-axis movement sliding block 5-7 includes the carrier one being fixedly connected with link 5-8, the carrying
Idler wheel one, the idler wheel two for rolling cooperation with the upper surfaces X-axis sliding rail 5-6, leading flank and trailing flank respectively are connected on frame one
With idler wheel three;Upper and lower part in X-axis gear mounting bracket 5-10 is rotationally equipped with X-axis driving gear 5-3 and X-axis respectively
Pass through synchronous tooth profile band connection between driven gear 5-2, X-axis driving gear 5-3 and X-axis driven gear 5-2;The X-axis sliding
Gear 5-4 and X-axis driven gear 5-2 are co-axially mounted on the lower part on the inside of X-axis gear mounting bracket 5-10, and with X-axis slide teeth
Wheel 5-5 engagements;The X-axis servo motor 5-1 be mounted on X-axis gear mounting bracket 5-10 upper outside, and with X-axis driving tooth
5-3 is taken turns to be drivingly connected;
The cooler 5-9 includes cooling shell, and the cooling enclosure interior is by being separately positioned on the two of upper and lower part
A partition board 5-9-4 is divided into three parts, and respectively two positioned at the heat-exchanging chamber 5-9-3 at middle part and below and above are slow
Rush process chamber 5-9-5;The upper, middle and lower of the heat-exchanging chamber 5-9-3 be respectively arranged be connected to its inner cavity it is cold
But liquid exports 5-9-7, medicament inlet 5-9-8 and by coolant liquid entrance 5-9-1, the interior central area of heat-exchanging chamber 5-9-3
The top and bottom for being fixedly installed more heat-exchange tubes 5-9-2, more heat-exchange tube 5-9-2 are respectively penetrated positioned at top under
Two buffered room 5-9-5 in portion, preferably, the quantity of heat-exchange tube 5-9-2 is 20, more heat-exchange tube 5-9-2
Vertical equidistant arrangement;Two buffered room 5-9-5 of upper and lower part are respectively arranged with the refrigerant inlet being connected to its inner cavity
5-9-6 and refrigerant exit 5-9-9;Cooler 5-9 is fixed at outside the X-axis electric machine casing of X-axis servo motor 5-1, the X
Spindle motor shell is the hollow structure with inner cavity, and X-axis electric machine casing is connected with the inlet pipe being connected to its inner cavity and goes out
Liquid pipeline;The inlet pipe is connect with by coolant liquid outlet 5-9-7, the input end connection of the outlet tube road and water pump, water
The outlet end of pump is connect with by coolant liquid entrance 5-9-1;
Refrigerant enters buffered room 5-9-5 from refrigerant inlet 5-9-6, and then enters inside heat-exchange tube 5-9-2, will
Heat absorption caused by heat-exchange tube 5-9-2, and flowed out from refrigerant exit 5-9-9, the injection of refrigerant can be injected by pump;Quilt
Coolant liquid enters heat-exchanging chamber 5-9-3 by the effect of water pump from by coolant liquid entrance 5-9-1, transfers heat to heat-exchange tube
5-9-2, and X-axis electric machine casing is entered by the inlet pipe on X-axis electric machine casing again from by coolant liquid outlet 5-9-7 outflows
In inner cavity;External agent can be controllably added to by medicament inlet 5-9-8 inside heat-exchanging chamber 5-9-3, can be convenient for and quilt
Coolant liquid is reacted, to improve cooling effect.
The left and right sides of the crossbeam 10 has been respectively fixedly connected with horizontally disposed Y-axis sliding rail 6-6 and has stated Y-axis sliding
Gear bar 6-5;It is slidably provided with Y-axis sliding equipment 6 on the top of crossbeam 10;The Y-axis sliding equipment 6 includes Y-axis gear
Mounting bracket 6-9, Y-axis movement sliding block 6-7, Y-axis balladeur train 6-4 and Y-axis servo motor 6-1;Y-axis movement the sliding block 6-7 and Y
Shaft gear mounting bracket 6-9 is respectively distributed to the left and right sides difference of crossbeam 10, and passes through connecting plate 6-8 and Y-axis gear mounting bracket
6-9 is fixedly connected;The Y-axis movement sliding block 6-7 and Y-axis sliding rail 6-6 is slidably matched, and the Y-axis moves sliding block 6-7 packets
Include the carrying two being fixedly connected with connecting plate 6-8, be connected on the carrier two respectively with the upper surfaces Y-axis sliding rail 6-6,
Left side and right side roll idler wheel four, idler wheel five and the idler wheel six of cooperation;It can turn respectively in the Y-axis gear mounting bracket 6-9
It is equipped between Y-axis driving gear 6-3 and Y-axis driven gear 6-2, Y-axis driven gear 6-2 and Y-axis driving gear 6-3 and leads to dynamicly
Cross synchronous tooth profile band connection;The Y-axis balladeur train 6-4 and Y-axis driven gear 6-2 is co-axially mounted on Y-axis gear mounting bracket
The inside of 6-9, and engaged with Y-axis balladeur train 6-5;The Y-axis servo motor 6-1 is mounted on Y-axis gear mounting bracket 6-9's
Outside, and be drivingly connected with Y-axis driving gear 6-3;
The cutting nozzle 7-7 is set to the left side of Z-axis lifting mechanism 7, and the Z-axis lifting mechanism 7 includes Z axis mounting bracket 7-
5, screw rod 7-3, Z axis servo motor 7-1 and sliding pair 7-2;The Z axis mounting bracket 7-5 is pushed up by top plate 7-4, bottom plate 7-9, connection
The side end panel 7-8 of left end and it is connected to the postive stop baffle 7-6 compositions of the rear and front ends side end panel 7-8 between plate 7-4 and bottom plate 7-9;
The screw rod 7-3 is rotatably connected between top plate 7-4 and bottom plate 7-9;The Z axis servo motor 7-1 is fixed at top plate 7-4
Top, and its output shaft penetrate rotatably top plate 7-4 after connect with the upper end of screw rod 7-3;The sliding pair 7-2 slidings setting
Between two postive stop baffle 7-6, and its center offers threaded hole;Sliding pair 7-2 is set in screw rod 7-3 by screw-thread fit
Outside;The strip-shaped hole being longitudinally extended is provided in the middle part of side end panel 7-8;Pass through between the cutting nozzle 7-7 and sliding pair 7-2
The connecting rod for sliding through strip-shaped hole is fixedly connected;Two postive stop baffle 7-6 move sliding block away from the side of side end panel 7-8 and Y-axis
6-7 is fixedly connected;
The temperature of flame when in order to improve cutting, to improve cutting speed and cut quality, the cutting nozzle 7-7 includes cutting
Torch tip shell 7-7-10 and the mixing chamber 7-7-3, the cutting nozzle shell 7- in cutting nozzle shell 7-7-10 center of inside are set
The surrounding of 7-10 is provided with a large amount of through-holes;The lower end of the cutting nozzle shell 7-7-10 has flame jet 7-7-1, cutting nozzle shell
The inner part of body 7-7-10 is being fixedly installed igniter 7-7-2 close to the position of flame jet 7-7-1;The one of acetylene hose 7-7-9
End is by penetrating and being connect with the upper open end of mixing chamber 7-7-3, the other end of acetylene hose 7-7-9 at the top of cutting nozzle shell 7-7-10
It is connect with positioned at external acetylene source of supply;One end of oxygen hose 7-7-8 penetrates in acetylene hose 7-7-9 and is fixedly connected in end
Aerobic qi leel dissipates mouth 7-7-12, and the other end of oxygen hose 7-7-8 is connect with positioned at external oxygen supply source;Cutting temperature senses
Device is fixed on the outside of flame jet 7-7-1;The oxygen dispersion mouth 7-7-12 includes oxygen dispersion mouth shell, the oxygen
Upper end, the lower end of dispersion mouth shell are respectively arranged with oxygen inlet 7-7-12-8, oxygen dispersion mouth 7-7-12-2;Disperse in oxygen
Mouth enclosure interior shaft core position is disposed with oxygen and accelerates rotation cardan shaft 7-7-12-7, speedup fan room 7-7- from top to bottom
12-6, oxygen accelerating chamber 7-7-12-5, surge chamber 7-7-12-4 and oxygen spray pipe 7-7-12-3;Speedup fan room 7-7-12-
6, oxygen accelerating chamber 7-7-12-5, surge chamber 7-7-12-4 and oxygen spray pipe 7-7-12-3 are the tubular knot of upper and lower opening
Structure, and be fixedly connected with the madial wall of oxygen dispersion mouth shell by the connecting rod being radially arranged;Accelerate rotation cardan shaft 7-7-
The upper end of 12-7 is connect with the propulsion driving motor output shaft for being fixed at oxygen dispersion mouth shell upper end center, accelerates rotation
The lower end of cardan shaft 7-7-12-7 is stretched into speedup fan room 7-7-12-6 and is drivingly connected with speedup fan 7-7-12-11;Oxygen
The upper end of gas accelerating chamber 7-7-12-5 is fixedly connected with the lower end of speedup fan room 7-7-12-6, oxygen accelerating chamber 7-7-12-5 with
The upper end of surge chamber 7-7-12-4 connects, and the lower end of surge chamber 7-7-12-4 is fixed with the upper end of oxygen spray pipe 7-7-12-3 to be connected
It connects;The internal diameter of oxygen spray pipe 7-7-12-3 is less than the internal diameter of surge chamber 7-7-12-4;In oxygen accelerating chamber 7-7-12-5 and delay
The junction for rushing room 7-7-12-4 is provided with air door 7-7-12-12, is arranged in external air damper controller 7-7-12-9 and air door
7-7-12-12 control connections;It is internally provided with wind speed inductor 7-7-12-10 in surge chamber 7-7-12-4;Oxygen spray pipe 7-7-
The surface of 12-3 is provided with a large amount of through-holes;The upper end for disperseing mouth shell in oxygen is provided with multiple acetylene flow-disturbings hole 7-7-12-1;
Mixing chamber 7-7-3 can mix oxygen by a certain percentage with acetylene.It can be convenient for surveying in real time by cutting temperature sensor
Measure the temperature of cutting flame.
Oxygen enters oxygen from oxygen inlet 7-7-12-8 and disperses mouth 7-7-10, at the same time, driving motor is promoted to pass through
Oxygen accelerates rotation cardan shaft 7-7-12-7 to drive speedup fan 7-7-12-11 high speed rotations so that oxygen is in speedup fan room
7-7-12-6 obtains kinetic energy, and oxygen passes through oxygen accelerating chamber 7-7-12-5, and enters surge chamber 7-7- by air door 7-7-12-12
12-4, since oxygen spray pipe 7-7-12-3 bores become smaller suddenly, pressure increases so that oxygen will be from oxygen spray pipe 7-7-
It is sprayed in 12-3 through-holes;Since the flow-disturbing of acetylene flow-disturbing hole 7-7-12-1 acts on so that oxygen disperses the second outside mouth 7-7-10
Alkynyl moiety enters in oxygen dispersion mouth 7-7-12-2, and mixer is generated with oxygen mix;At the same time, by air damper controller
The controllable adjustment to oxygen flow is realized in the control of 7-7-12-9.
The igniter 7-7-2, promote driving motor, air damper controller 7-7-12-9, wind speed inductor 7-7-12-10,
Cutting temperature sensor, X-axis servo motor 5-1, Y-axis servo motor 6-1, Z axis servo motor 7-1 and water pump with controller 8
Connection.It is solid cylinder that the oxygen, which accelerates rotation cardan shaft 7-7-12-7,.
In order to enable the temperature higher of cutting flame, preferably to ensure cutting effect, the cutting nozzle shell 7-7-
It is fixedly connected with interior cover body 7-7-11 inside 10, forms tempering channel 7- between interior cover body 7-7-11 and cutting nozzle shell 7-7-10
The lower end of 7-4, tempering channel 7-7-4 are connected to flame jet 7-7-1, are tempered the upper end of channel 7-7-4 by being tempered valve 7-7-7
It is connect with entrance of the fixing sleeve loaded on the heat exchanger 7-7-6 outside acetylene hose 7-7-9, the outlet of heat exchanger 7-7-6 extends
To outside cutting nozzle shell 7-7-10.In this way, the after-heat that flame jet 7-7-1 combustion tail gas generates can pass through heat exchange
Device 7-7-6 preheats oxygen hose 7-7-8, meanwhile, it can also reduce the temperature of efflux gas.
For the ease of realizing the control of accurate cutting position, the left and right ends of the X-axis sliding rail 5-6 be both provided with
X-axis moves the matched X-axis Overstroke detector in the left and right ends sliding block 5-7;The left and right ends of the Y-axis sliding rail 6-6
It is both provided with and moves the matched Y-axis Overstroke detector in the left and right ends sliding block 6-7 with Y-axis;The Y-axis gear mounting bracket 6-
Speed probe for detecting Y-axis driving gear 6-3 rotating speeds is installed in 9;Opposite the one of the top plate 7-4 and bottom plate 7-9
Side is mounted on and the matched Z axis Overstroke detector of the upper and lower ends of sliding pair;The X-axis Overstroke detector, Y
Axis Overstroke detector, speed probe and Z axis Overstroke detector are connect with controller 8.
In order to ensure that the temperature of cutting flame, the outer side covering on the tops cutting nozzle shell 7-7-10 have insulating layer 7-7-
5。
For the ease of adjusting the height of supporting rack, to realize that the adjustment of height of table, support frame as described above 1 have four branch
The bottom of leg, every supporting leg is both provided with height-adjustable adjustable angled seat.
Support frame as described above 1 is formed by stainless steel tube welding production, and the thickness of stainless steel tube is 5cm~8cm;The X-axis is slided
Dynamic rail road 5-6 materials are nickel-clad steel plate, and thickness is 1cm~3cm;The Y-axis sliding rail 6-6 materials are nickel-clad steel plate,
Thickness is 1cm~3cm;The distance between the reject chute 3 and workbench 4 are 10cm~15cm;The flame jet 7-7-1 is in
Truncated conical shape;The mixing chamber 7-7-3 is in coniform.
The insulating layer 7-7-5 is made of high molecular material.
The oxygen spray pipe 7-7-12-3 is composed of the following components by ratio of weight and the number of copies:
338.7~563.8 parts of purified water, 2- methyl-pentadecanoic acid -2- ethyls -2- [[(2- methyl-1s-oxo pentadecyl)
Oxygen] methyl generation] 130.6~172.4 parts of 1,3- propylidene ester, 4- methoxyl groups-α-[[methyl sulphonyl] oxygroup] imino group]-benzene
133.8~242.9 parts of base acetonitrile, 3- (methyl mercapto) -129.8~146.3 parts of butyraldehyde, 132.1~189.2 parts of everbright red toner C, (1-
Methyl ethylidene) bis- (4,1- phenoxy group -2,1- ethylidene) 135.3~196.7 parts of diacetates, molybdenum nanoparticle 137.4~
192.3 parts, 130.0~172.0 parts of the polymer of newtrex and alpha -hydro-omega -hydroxypoly (oxidation -1,2- second diyl), formaldehyde
With 132.0~172.4 parts of the polymer of [complex compound of 4- (1,1- dimethyl ethyl) phenol and magnesia], alkali formula aluminium hydroxyacetate
132.3~155.9 parts, 121.5~157.0 parts of the polymethylene polyphenylene isocyanates of methyl ethyl ketoxime sealing end, 2- methyl is pungent
120.3~163.4 parts of aldehyde, 129.5~174.1 parts of formic acid -4- cyclo-octene -1- alcohol esters, polyurethane elastomer 139.8~183.6
Part, mass concentration is 162.5~216.4 parts of the hexadecanyl phosphate fatting agent of 129ppm~396ppm.
In order to which the resistance to compression and resistance to deformation intensity that make oxygen spray pipe 7-7-12-3 are more preferable, the oxygen spray pipe 7-7-12-3
Production method it is as follows:
S1:In energy-saving type stirred reactor, purified water and 2- methyl-pentadecanoic acid -2- ethyls -2- [[(2- methyl-is added
1- oxos pentadecyl) oxygen] methyl generation] 1,3- propylidene esters, start the blender in energy-saving type stirred reactor, setting speed
For 131rpm~177rpm;Start energy-saving type stirred reactor in steam coil heater, make temperature rise to 146.7 DEG C~
147.8 DEG C, 4- methoxyl groups-α-[[methyl sulphonyl] oxygroup] imino group is added]-phenylacetonitrile stirs evenly, organic matter is made
Ⅰ;
S2:It is 122.7m that organic matter made from S1 I, which is passed through flow,3/ min~163.3m3The xenon 123.6 of/min~
134.4 minute;The pH value for adjusting solution in energy-saving type stirred reactor is 4.1~8.2, keeps the temperature 123.1~363.1 minutes;It crosses
Filter, removal impurity, obtain suspension;
S3:Polymerizeing for formaldehyde and [complex compound of 4- (1,1- dimethyl ethyls) phenol and magnesia] is added in S2 suspension
Object, adjustment pH value form sediment purifying water elution between 1.5~2.0;Solid content is obtained by centrifuge, high temperature is dry
It is dry, 0.882 × 10 is crossed after grinding3Mesh sieves;Obtain the mixture of character change;
S4:The mixture that character made from S3 is changed adds to the methyl ethyl ketoxime that mass concentration is 133ppm~363ppm
In the polymethylene polyphenylene isocyanates of sealing end;Start the steam coil heater in energy-saving type stirred reactor, setting
Energy-saving type stirred reactor operating parameter is:Temperature is 207.8 DEG C~263.3 DEG C;PH is adjusted between 4.1~8.1;Pressure is
1.29MPa~1.3MPa;Reaction time is 0.4~0.9 hour;After reaction, it is depressurized to zero gauge pressure, is discharged into molding press,
Obtain oxygen spray pipe 7-7-12-3.
It is the embodiment of the manufacturing process of oxygen spray pipe 7-7-12-3 of the present invention below, embodiment is in order into one
Step illustrates present disclosure, but should not be construed as limiting the invention.In the situation without departing substantially from spirit of that invention and essence
Under, to changing and replacing made by the method for the present invention, step or condition, all belong to the scope of the present invention.
Unless otherwise specified, the conventional means that technological means used in embodiment is well known to those skilled in the art.
The content that following embodiment further illustrates the present invention, as oxygen spray pipe 7-7-12-3, it is of the invention
Significant components increase the service life of integral device due to its presence, it sends out for the safety of integral device, even running
Wave key effect.For this purpose, by it is following be embodiment, further verify oxygen spray pipe 7-7-12-3 of the present invention,
The physical characteristic higher than other related patents shown.
Embodiment 1
Oxygen spray pipe 7-7-12-3 of the present invention is prepared according to the following steps, and is counted in parts by weight:
1st step:In energy-saving type stirred reactor, 338.7 parts of purified water and 2- methyl-pentadecanoic acid -2- ethyls -2- is added
[[(2- methyl-1s-oxo pentadecyl) oxygen] methyl generation] 130.6 parts of 1,3- propylidene ester starts in energy-saving type stirred reactor
Blender, setting speed 131rpm, start energy-saving type stirred reactor in steam coil heater, so that temperature is risen to
146.7 DEG C, 4- methoxyl groups-α-[[methyl sulphonyl] oxygroup] imino group is added] 133.8 parts of-phenylacetonitrile stirs evenly, carries out
3- (methyl mercapto) -129.8 parts of butyraldehyde is added in reaction 123.6 minutes, and it is 122.7m to be passed through flow3The xenon 123.6 of/min is divided
Clock;132.1 parts of everbright red toner C, the steaming being again started up in energy-saving type stirred reactor is added in energy-saving type stirred reactor later
Vapour spiral heater makes temperature rise to 163.8 DEG C, keeps the temperature 123.8 minutes, and (1- methyl ethylidene) bis- (4,1- phenoxy groups-are added
2,1- ethylidene) 135.3 parts of diacetate, the pH value for adjusting solution in energy-saving type stirred reactor is 4.1, keeps the temperature 123.1 points
Clock;
2nd step:Separately take 137.4 parts of molybdenum nanoparticle, by molybdenum nanoparticle power be 6.63KW under ultrasonication
After 0.129 hour;Molybdenum nanoparticle is added in another energy-saving type stirred reactor, it is 133ppm's that mass concentration, which is added,
130.0 parts of dispersed molybdenum nanoparticles of polymer of newtrex and alpha -hydro-omega -hydroxypoly (oxidation -1,2- second diyl), start section
Steam coil heater in energy formula stirred reactor, makes solution temperature at 44 DEG C, starts stirring in energy-saving type stirred reactor
Machine is mixed, and with 4 × 102The speed of rpm stirs, and adjustment pH value is 4.5, insulated and stirred 129 minutes;Stop reaction later to stand
6.63 × 10 minutes, filtering, removal impurity;Formaldehyde and [4- (1,1- dimethyl ethyls) phenol and magnesia is added in suspension
Complex compound] 132.0 parts of polymer, adjustment pH value forms sediment purifying water elution, turned by centrifuge 1.5
Speed 4.882 × 103Solid content is obtained under rpm, 2.657 × 102It is dry at a temperature of DEG C, 0.882 × 10 is crossed after grinding3Mesh sieves, standby
With;
3rd step:Another molybdenum nanoparticle after taking alkali formula aluminium hydroxyacetate 132.3 and the processing of the 2nd step, uses acute angle after mixing
Dissipate the irradiation of gamma-rays diffraction, the energy that acute angle dissipates gamma-rays diffraction irradiation is 120.3MeV, dosage 168.3kGy, irradiation time
It is 132.3 minutes, obtains the alkali formula aluminium hydroxyacetate and molybdenum nanoparticle mixture of character change;Alkali formula aluminium hydroxyacetate and molybdenum are received
Rice particle mixture is placed in another energy-saving type stirred reactor, starts the steam-coil-heater in energy-saving type stirred reactor
Device, 131.5 DEG C of set temperature start the blender in energy-saving type stirred reactor, and rotating speed 123rpm, pH are adjusted to 4.8, take off
Water 132.8 minutes, it is spare;
4th step:The alkali formula aluminium hydroxyacetate and molybdenum nanoparticle mixture that the character that 3rd step is obtained changes, add to quality
In 121.5 parts of the polymethylene polyphenylene isocyanates of the methyl ethyl ketoxime sealing end of a concentration of 133ppm, cocurrent adds to the 1st step
In energy-saving type stirred reactor, flow acceleration 268mL/min;Start energy-saving type and be stirred to react mechanical stirrer, setting speed is
137rpm;Stirring 4 minutes;120.3 parts of 2 methyl octylaldehyde is added, the steam-coil-heater in energy-saving type stirred reactor is started
Device is warming up to 167.5 DEG C, and pH is adjusted to 4.5, and it is 122.367m to be passed through xenon ventilatory capacity3/ min, heat preservation stand 157.7 minutes;
It being again started up energy-saving type and is stirred to react mechanical stirrer, 129.5 parts of formic acid -4- cyclo-octene -1- alcohol esters are added in rotating speed 132rpm,
And pH is made to be adjusted to 4.5, heat preservation stands 156.6 minutes;
5th step:Start the blender in energy-saving type stirred reactor, setting speed 129rpm starts energy-saving type stirring
Steam coil heater in reactor sets temperature in energy-saving type stirred reactor as 1.70 × 102DEG C, polyurethane is added
139.8 parts of elastomer reacts 123.8 minutes;The hexadecanyl phosphate fatting agent that mass concentration is 129ppm is added later
162.5 parts, start the steam coil heater in energy-saving type stirred reactor, set temperature in energy-saving type stirred reactor as
207.8 DEG C, pH is adjusted to 4.1, and pressure 1.29MPa, the reaction time is 0.4 hour;It is 0MPa, cooling to be depressurized to gauge pressure later
It discharges to 123.8 DEG C into molding press to get to oxygen spray pipe 7-7-12-3;
The grain size of the molybdenum nanoparticle is 137 μm.
Embodiment 2
Oxygen spray pipe 7-7-12-3 of the present invention is prepared according to the following steps, and is counted in parts by weight:
1st step:In energy-saving type stirred reactor, 563.8 parts of purified water and 2- methyl-pentadecanoic acid -2- ethyls -2- is added
[[(2- methyl-1s-oxo pentadecyl) oxygen] methyl generation] 172.4 parts of 1,3- propylidene ester starts in energy-saving type stirred reactor
Blender, setting speed 177rpm, start energy-saving type stirred reactor in steam coil heater, so that temperature is risen to
147.8 DEG C, 4- methoxyl groups-α-[[methyl sulphonyl] oxygroup] imino group is added] 242.9 parts of-phenylacetonitrile stirs evenly, carries out
3- (methyl mercapto) -146.3 parts of butyraldehyde is added in reaction 134.4 minutes, and it is 163.3m to be passed through flow3The xenon 134.4 of/min is divided
Clock;189.2 parts of everbright red toner C, the steaming being again started up in energy-saving type stirred reactor is added in energy-saving type stirred reactor later
Vapour spiral heater makes temperature rise to 196.9 DEG C, keeps the temperature 134.3 minutes, and (1- methyl ethylidene) bis- (4,1- phenoxy groups-are added
2,1- ethylidene) 196.7 parts of diacetate, the pH value for adjusting solution in energy-saving type stirred reactor is 8.2, keeps the temperature 363.1 points
Clock;
2nd step:Separately take 192.3 parts of molybdenum nanoparticle, by molybdenum nanoparticle power be 12.07KW under ultrasonication
1.196 after hour;Molybdenum nanoparticle is added in another energy-saving type stirred reactor, it is 363ppm's that mass concentration, which is added,
172.0 parts of dispersed molybdenum nanoparticles of polymer of newtrex and alpha -hydro-omega -hydroxypoly (oxidation -1,2- second diyl), start section
Steam coil heater in energy formula stirred reactor, makes solution temperature between 83 DEG C, starts in energy-saving type stirred reactor
Blender, and with 8 × 102The speed of rpm stirs, and adjustment pH value is 8.0, insulated and stirred 196 minutes;It is quiet to stop reaction later
It sets 12.07 × 10 minutes, filtering, removal impurity;Formaldehyde and [4- (1,1- dimethyl ethyls) phenol and oxidation is added in suspension
The complex compound of magnesium] 172.4 parts of polymer, adjustment pH value forms sediment purifying water elution, existed by centrifuge 2.0
Rotating speed 9.728 × 103Solid content is obtained under rpm, 3.430 × 102It is dry at a temperature of DEG C, 1.728 × 10 are crossed after grinding3Mesh sieves,
It is spare;
3rd step:Another molybdenum nanoparticle after taking 155.9 parts of alkali formula aluminium hydroxyacetate and the processing of the 2nd step, uses sharp after mixing
Angle dissipates the irradiation of gamma-rays diffraction, the energy that acute angle dissipates gamma-rays diffraction irradiation is 148.4MeV, dosage 208.4kGy, irradiation when
Between be 157.4 minutes, obtain character change alkali formula aluminium hydroxyacetate and molybdenum nanoparticle mixture;By alkali formula aluminium hydroxyacetate and molybdenum
Nanoparticle mixture is placed in another energy-saving type stirred reactor, starts the steam-coil-heater in energy-saving type stirred reactor
Device, 177.1 DEG C of set temperature start the blender in energy-saving type stirred reactor, and rotating speed 518rpm, pH are adjusted to 8.6, take off
Water 146.6 minutes, it is spare;
4th step:The alkali formula aluminium hydroxyacetate and molybdenum nanoparticle mixture that the character that 3rd step is obtained changes, add to quality
In 157.0 parts of the polymethylene polyphenylene isocyanates of the methyl ethyl ketoxime sealing end of a concentration of 363ppm, cocurrent adds to the 1st step
In energy-saving type stirred reactor, flow acceleration 996mL/min;Start energy-saving type and be stirred to react mechanical stirrer, setting speed is
177rpm;Stirring 8 minutes;163.4 parts of 2 methyl octylaldehyde is added, the steam-coil-heater in energy-saving type stirred reactor is started
Device is warming up to 204.4 DEG C, and pH is adjusted to 8.4, and it is 163.400m to be passed through xenon ventilatory capacity3/ min, heat preservation stand 187.8 minutes;
It being again started up energy-saving type and is stirred to react mechanical stirrer, 174.1 parts of formic acid -4- cyclo-octene -1- alcohol esters are added in rotating speed 177rpm,
And pH is made to be adjusted to 8.4, heat preservation stands 196.4 minutes;
5th step:Start the blender in energy-saving type stirred reactor, setting speed 196rpm starts energy-saving type stirring
Steam coil heater in reactor sets temperature in energy-saving type stirred reactor as 2.972 × 102DEG C, poly- ammonia is added
183.6 parts of ester elastomer reacts 134.9 minutes;The hexadecanyl phosphate fatting agent that mass concentration is 396ppm is added later
216.4 parts, start the steam coil heater in energy-saving type stirred reactor, set temperature in energy-saving type stirred reactor as
263.3 DEG C, pH is adjusted to 8.1, and pressure 1.3MPa, the reaction time is 0.9 hour;It is 0MPa, cooling to be depressurized to gauge pressure later
It discharges to 134.9 DEG C into molding press to get to oxygen spray pipe 7-7-12-3;
The grain size of the molybdenum nanoparticle is 147 μm.
Embodiment 3
Oxygen spray pipe 7-7-12-3 of the present invention is prepared according to the following steps, and is counted in parts by weight:
1st step:In energy-saving type stirred reactor, 338.9 parts of purified water and 2- methyl-pentadecanoic acid -2- ethyls -2- is added
[[(2- methyl-1s-oxo pentadecyl) oxygen] methyl generation] 130.9 parts of 1,3- propylidene ester starts in energy-saving type stirred reactor
Blender, setting speed 131rpm, start energy-saving type stirred reactor in steam coil heater, so that temperature is risen to
146.9 DEG C, 4- methoxyl groups-α-[[methyl sulphonyl] oxygroup] imino group is added] 133.9 parts of-phenylacetonitrile stirs evenly, carries out
3- (methyl mercapto) -129.9 parts of butyraldehyde is added in reaction 123.9 minutes, and it is 122.9m to be passed through flow3The xenon 123.9 of/min is divided
Clock;132.9 parts of everbright red toner C, the steaming being again started up in energy-saving type stirred reactor is added in energy-saving type stirred reactor later
Vapour spiral heater makes temperature rise to 163.9 DEG C, keeps the temperature 123.9 minutes, and (1- methyl ethylidene) bis- (4,1- phenoxy groups-are added
2,1- ethylidene) 135.9 parts of diacetate, the pH value for adjusting solution in energy-saving type stirred reactor is 4.9, keeps the temperature 123.9 points
Clock;
2nd step:Separately take 137.9 parts of molybdenum nanoparticle, by molybdenum nanoparticle power be 6.639KW under ultrasonication
After 0.1299 hour;Molybdenum nanoparticle is added in another energy-saving type stirred reactor, mass concentration, which is added, is
130.9 parts of dispersed molybdenum nanometers of polymer of the newtrex and alpha -hydro-omega -hydroxypoly (oxidation -1,2- second diyl) of 133.9ppm
Particle starts the steam coil heater in energy-saving type stirred reactor, makes solution temperature at 44.9 DEG C, starts energy-saving type stirring
Blender in reactor, and with 4.9 × 102The speed of rpm stirs, and adjustment pH value is 4.9, insulated and stirred 129.9 minutes;It
Stop reaction afterwards and stands 6.63 × 10 minutes, filtering, removal impurity;Formaldehyde and [4- (1,1- dimethyl second is added in suspension
Base) phenol and magnesia complex compound] 132.9 parts of polymer, adjustment pH value forms sediment purifying water elution 1.9,
By centrifuge in rotating speed 4.882 × 103Solid content is obtained under rpm, 2.657 × 102It is dry at a temperature of DEG C, mistake after grinding
0.882×103Mesh sieves, spare;
3rd step:Another molybdenum nanoparticle after taking alkali formula aluminium hydroxyacetate 132.9 and the processing of the 2nd step, uses acute angle after mixing
Dissipate the irradiation of gamma-rays diffraction, the energy that acute angle dissipates gamma-rays diffraction irradiation is 120.9MeV, dosage 168.9kGy, irradiation time
It is 132.9 minutes, obtains the alkali formula aluminium hydroxyacetate and molybdenum nanoparticle mixture of character change;Alkali formula aluminium hydroxyacetate and molybdenum are received
Rice particle mixture is placed in another energy-saving type stirred reactor, starts the steam-coil-heater in energy-saving type stirred reactor
Device, 131.9 DEG C of set temperature start the blender in energy-saving type stirred reactor, and rotating speed 123rpm, pH are adjusted to 4.9, take off
Water 132.9 minutes, it is spare;
4th step:The alkali formula aluminium hydroxyacetate and molybdenum nanoparticle mixture that the character that 3rd step is obtained changes, add to quality
In 121.9 parts of the polymethylene polyphenylene isocyanates of the methyl ethyl ketoxime sealing end of a concentration of 133.9ppm, cocurrent adds to the 1st step
Energy-saving type stirred reactor in, flow acceleration 268.9mL/min;Start energy-saving type and be stirred to react mechanical stirrer, setting turns
Speed is 137rpm;Stirring 4.9 minutes;120.9 parts of 2 methyl octylaldehyde is added, the steam disc in energy-saving type stirred reactor is started
Pipe heater is warming up to 167.9 DEG C, and pH is adjusted to 4.9, and it is 122.9m to be passed through xenon ventilatory capacity3/ min, heat preservation stand 157.9
Minute;It is again started up energy-saving type and is stirred to react mechanical stirrer, formic acid -4- cyclo-octene -1- alcohol esters are added in rotating speed 132rpm
129.9 parts, and pH is made to be adjusted to 4.9, heat preservation stands 156.9 minutes;
5th step:Start the blender in energy-saving type stirred reactor, setting speed 129rpm starts energy-saving type stirring
Steam coil heater in reactor sets temperature in energy-saving type stirred reactor as 1.70 × 102DEG C, polyurethane is added
139.9 parts of elastomer reacts 123.9 minutes;The hexadecanyl phosphate fatting agent that mass concentration is 129ppm is added later
162.5 parts, start the steam coil heater in energy-saving type stirred reactor, set temperature in energy-saving type stirred reactor as
207.9 DEG C, pH is adjusted to 4.9, and pressure 1.29MPa, the reaction time is 0.41 hour;It is 0MPa, drop to be depressurized to gauge pressure later
Temperature discharges into molding press to get to oxygen spray pipe 7-7-12-3 to 123.9 DEG C;
The grain size of the molybdenum nanoparticle is 137 μm.
Reference examples
Reference examples are tested for the property experiment using the oxygen spray pipe of certain commercially available brand.
Embodiment 4
The oxygen spray pipe that Examples 1 to 3 and reference examples are obtained is tested for the property experiment, is fought after test
The parameters such as Compressive Strength enhancing rate, resistance to deformation strength enhancing rate, partition board service life enhancing rate, impact resistance enhancing rate are divided
Analysis.Data analysis is as shown in table 1.
As seen from Table 1, oxygen spray pipe 7-7-12-3 of the present invention, compression strength enhancing rate, resistance to deformation intensity
Enhancing rate, oxygen spray pipe service life enhancing rate, impact resistance enhancing rate are above the product of prior art production.
In addition, as shown in figure 8, oxygen spray pipe of the present invention is carried out with reference examples, become with usage time
Change test data statistics.Find out in figure, Examples 1 to 3 is substantially better than the production of prior art production in determination techniques index
Product.
A kind of course of work of residents in rural community processing equipment with oxygen dispersion mouth in the present invention is:
1st step:Desiccation house refuse block etc. to be cut is placed on workbench 4 by staff, solid with fixing device
It sets;Staff powers on, and the coordinate A (X, Y, Z) corresponding to cutting track is inputted on controller 8;Press controller 8
On start button, X-axis sliding equipment 5, Y-axis sliding equipment 6, Z-axis lifting mechanism 7 are moved according to corresponding coordinate;
2nd step:In 5 moving process of X-axis sliding equipment, the 5-1 driving X-axis driving gear 5-3 rotations of X-axis servo motor, X
Axis driving gear 5-3 drives the 5-2 rotations of X-axis driven gear by timing belt, to drive X-axis balladeur train 5-4 in X-axis
It is moved on balladeur train 5-5;X-axis moves sliding block 5-7 in the case where X-axis driven gear 5-2 drives, and is done along X-axis sliding rail 5-6 past
Multiple sliding motion;In X-axis moves sliding block 5-7 sliding processes, sliding of the X-axis Overstroke detector to X-axis movement sliding block 5-7
Distance monitoring in real time, when X-axis Overstroke detector detects that the sliding distance of X-axis movement sliding block 5-7 reaches X, X-axis stroke
Feedback signal is sent to controller 8 to bit detector, controller 8 stops X-axis servo motor 5-1;
3rd step:In 6 moving process of Y-axis sliding equipment, the 6-1 driving Y-axis driving gear 6-3 rotations of Y-axis servo motor, Y
Axis driving gear 6-3 drives the 6-2 rotations of Y-axis driven gear by timing belt, to drive Y-axis balladeur train 6-4 in Y-axis
It is moved on balladeur train 6-5;Y-axis moves sliding block 6-7 in the case where Y-axis driven gear 6-2 drives, and is done along Y-axis sliding rail 6-6 past
Multiple sliding motion;In Y-axis moves sliding block 6-7 sliding processes, sliding of the Y-axis Overstroke detector to Y-axis movement sliding block 6-7
Distance monitoring in real time, when Y-axis Overstroke detector detects that the sliding distance of Y-axis movement sliding block 6-7 reaches Y, Y-axis stroke
Feedback signal is sent to controller 8 to bit detector, controller 8 stops Y-axis servo motor 6-1;
4th step:In 7 lifting process of Z-axis lifting mechanism, Z axis servo motor 7-1 drives sliding pair 7-2 on screw rod 7-3
It spins rotary motion, Z axis Overstroke detector 7-5 monitors the lifting distance of sliding pair 7-2 in real time, when Z axis stroke arrives
When bit detector detects that the lifting distance of sliding pair 7-2 reaches Z, feedback signal is sent to control by Z axis Overstroke detector
Device 8 processed, controller 8 stop Z axis servo motor 7-1;
5th step:Reject chute 3 is collected the waste material generated in cutting process, and extraction reject chute 3 can be cleared up.
The apparatus structure is simple, high degree of automation, and major advantage is that the little house refuse block of cutting thickness is dry
When changing block, cutting speed of the present invention is fast, especially when cutting riverbed sludge desiccation block, speed up to 5~6 times of oxygen cutting method,
Cut surface is bright and clean, thermal deformation is small, almost without heat affected area.The device carries out centralized control by controller 8, can accurately determine
Position, can cut object according to Grid Track, notch is smooth, and cutting speed is fast;It is controlled by controller 8, also
The device anti-interference ability can be made stronger, and have the function of certain automatic cutting gap compensation, work efficiency is high.
Claims (10)
1. a kind of residents in rural community processing equipment with oxygen dispersion mouth, including supporting rack (1), workbench (4) and cutting torch
Mouth (7-7), which is characterized in that further include reject chute (3), Y-axis sliding equipment (6), cooler (5-9) and controller (8), it is described
The fixed branch of workbench (4) is located at the upper end of supporting rack (1), and workbench (4) is by several equally distributed grids and connects adjacent
Connecting rod composition between grid;
A pair of of sliding slot (9) that left and right extends is provided with below workbench (4), a pair of of sliding slot (9), which is respectively fixedly connected with, to be supported
Front-end and back-end on the inside of frame (1);The reject chute (3) with a pair of of sliding slot (9) cooperation by being slidably arranged in workbench (4)
Lower section;Be provided with the balladeur train slided along its length above the workbench (4), the balladeur train by horizontal crossbeam (10) and
It is fixedly connected on vertical beam (10) composition of crossbeam (10) both ends lower part;It is provided with horizontal two on the outside of two vertical beams (10)
Slideway, two slideways are respectively fixedly connected with the front-end and back-end on workbench (4) top, and the slideway is by the X-axis positioned inside
Sliding rail (5-6) and positioned at outside X-axis balladeur train item (5-5) form;Two X being slidably matched respectively with two slideways
Axis sliding equipment (5) is respectively fixedly connected with the outside two vertical beam (10) lower ends;The X-axis sliding equipment (5) includes X-axis tooth
Take turns mounting bracket (5-10), X-axis movement sliding block (5-7), X-axis balladeur train (5-4) and X-axis servo motor (5-1), the X-axis tooth
It is fixedly connected by the link (5-8) above slideway between wheel mounting bracket (5-10) and vertical beam (10), the X-axis movement
Sliding block (5-7) is mounted on the inside of link (5-8), and is slidably matched with X-axis sliding rail (5-6);X-axis gear mounting bracket
Upper and lower part in (5-10) is rotationally equipped with X-axis driving gear (5-3) and X-axis driven gear (5-2), X-axis respectively
Pass through synchronous tooth profile band connection between driving gear (5-3) and X-axis driven gear (5-2);The X-axis balladeur train (5-4) and X
Axis driven gear (5-2) is co-axially mounted on the lower part on the inside of X-axis gear mounting bracket (5-10), and with X-axis balladeur train item (5-
5) it engages;The X-axis servo motor (5-1) be mounted on X-axis gear mounting bracket (5-10) upper outside, and with X-axis driving tooth
(5-3) is taken turns to be drivingly connected;
The cooler (5-9) includes cooling shell, and the cooling enclosure interior is by being separately positioned on two of upper and lower part
Partition board (5-9-4) is divided into three parts, respectively two positioned at the heat-exchanging chamber (5-9-3) at middle part and below and above
Buffered room (5-9-5);The upper, middle and lower of the heat-exchanging chamber (5-9-3) is respectively arranged with to be connected to its inner cavity
By coolant liquid outlet (5-9-7), medicament inlet (5-9-8) and by coolant liquid entrance (5-9-1), heat-exchanging chamber (5-9-3)
Interior central area be fixedly installed more heat-exchange tubes (5-9-2), the top and bottom point of more heat-exchange tubes (5-9-2)
Two buffered rooms (5-9-5) below and above are not penetrated;Two buffered rooms (5-9-5) of upper and lower part
It is respectively arranged with the refrigerant inlet (5-9-6) being connected to its inner cavity and refrigerant exit (5-9-9);Cooler (5-9) is fixedly installed
Outside the X-axis electric machine casing of X-axis servo motor (5-1), the X-axis electric machine casing is the hollow structure with inner cavity, and X-axis
Electric machine casing is connected with the inlet pipe being connected to its inner cavity and outlet tube road;The inlet pipe exports (5- with by coolant liquid
It 9-7) connects, the input end of the outlet tube road and water pump connects, and the outlet end of water pump connects with by coolant liquid entrance (5-9-1)
It connects;
It has been respectively fixedly connected with horizontally disposed Y-axis sliding rail (6-6) at left and right sides of the crossbeam (10) and has stated Y-axis sliding
Gear bar (6-5);It is slidably provided with Y-axis sliding equipment (6) on the top of crossbeam (10);The Y-axis sliding equipment (6) includes
Y-axis gear mounting bracket (6-9), Y-axis movement sliding block (6-7), Y-axis balladeur train (6-4) and Y-axis servo motor (6-1);The Y
Axis movement sliding block (6-7) and Y-axis gear mounting bracket (6-9) are respectively distributed to the left and right sides difference of crossbeam (10), and pass through company
Fishplate bar (6-8) is fixedly connected with Y-axis gear mounting bracket (6-9);The Y-axis movement sliding block (6-7) and Y-axis sliding rail (6-6)
It is slidably matched;It is rotationally equipped with Y-axis driving gear (6-3) respectively in the Y-axis gear mounting bracket (6-9) and Y-axis is driven
Gear (6-2) passes through synchronous tooth profile band connection between Y-axis driven gear (6-2) and Y-axis driving gear (6-3);The Y-axis is slided
Moving gear (6-4) is co-axially mounted on the inside of Y-axis gear mounting bracket (6-9) with Y-axis driving gear (6-3), and is slided with Y-axis
Gear bar (6-5) engages;The Y-axis servo motor (6-1) be mounted on Y-axis gear mounting bracket (6-9) outside, and with Y-axis master
Moving gear (6-3) is drivingly connected;
The cutting nozzle (7-7) is set to the left side of Z-axis lifting mechanism (7), and the Z-axis lifting mechanism (7) includes Z axis mounting bracket
(7-5), screw rod (7-3), Z axis servo motor (7-1) and sliding pair (7-2);The Z axis mounting bracket (7-5) by top plate (7-4),
The side end panel (7-8) of left end and before being connected to side end panel (7-8) between bottom plate (7-9), connection top plate (7-4) and bottom plate (7-9)
Postive stop baffle (7-6) composition at both ends afterwards;The screw rod (7-3) is rotatably connected between top plate (7-4) and bottom plate (7-9);Institute
State Z axis servo motor (7-1) and be fixed at the top top plate (7-4), and its output shaft penetrate rotatably top plate (7-4) afterwards with
The upper end of screw rod (7-3) connects;The sliding pair (7-2) is slideably positioned between two postive stop baffles (7-6), and its center is opened
Equipped with threaded hole;Sliding pair (7-2) is set in the outside of screw rod (7-3) by screw-thread fit;The middle part of side end panel (7-8) is arranged
There is the strip-shaped hole being longitudinally extended;It is solid by sliding through the connecting rod of strip-shaped hole between the cutting nozzle (7-7) and sliding pair (7-2)
Fixed connection;Two postive stop baffles (7-6) are fixedly connected away from the side of side end panel (7-8) with Y-axis movement sliding block (6-7);It is described
Cutting nozzle (7-7) includes the mixing chamber of cutting nozzle shell (7-7-10) and setting in cutting nozzle shell (7-7-10) center of inside
The surrounding of (7-7-3), the cutting nozzle shell (7-7-10) are provided with a large amount of through-holes;Under the cutting nozzle shell (7-7-10)
There is flame jet (7-7-1), the inner part of cutting nozzle shell (7-7-10) to be fixed in the position close to flame jet (7-7-1) at end
It is provided with igniter (7-7-2);One end of acetylene hose (7-7-9) is penetrated by cutting nozzle shell (7-7-10) top and and mixing chamber
The upper open end of (7-7-3) connects, and the other end of acetylene hose (7-7-9) is connect with positioned at external acetylene source of supply;Oxygen hose
The one end of (7-7-8) penetrates in acetylene hose (7-7-9) and is fixedly connected with oxygen dispersion mouth (7-7-12), oxygen hose in end
The other end of (7-7-8) is connect with positioned at external oxygen supply source;Cutting temperature sensor is fixed at flame jet (7-
7-1) outside;Oxygen dispersion mouth (7-7-12) includes oxygen dispersion mouth shell, the upper end of the oxygen dispersion mouth shell, under
End is respectively arranged with oxygen inlet (7-7-12-8), oxygen dispersion mouth (7-7-12-2);In oxygen dispersion mouth enclosure interior axle center
Position is disposed with oxygen and accelerates rotation cardan shaft (7-7-12-7), speedup fan room (7-7-12-6), oxygen from top to bottom
Accelerating chamber (7-7-12-5), surge chamber (7-7-12-4) and oxygen spray pipe (7-7-12-3);Speedup fan room (7-7-12-6),
Oxygen accelerating chamber (7-7-12-5), surge chamber (7-7-12-4) and oxygen spray pipe (7-7-12-3) are the tubular of upper and lower opening
Structure, and be fixedly connected with the madial wall of oxygen dispersion mouth shell by the connecting rod being radially arranged;Accelerate rotation cardan shaft (7-
Upper end 7-12-7) is connect with the propulsion driving motor output shaft for being fixed at oxygen dispersion mouth shell upper end center, is accelerated
The lower end of rotation cardan shaft (7-7-12-7) is stretched into speedup fan room (7-7-12-6) and is driven with speedup fan (7-7-12-11)
Dynamic connection;The upper end of oxygen accelerating chamber (7-7-12-5) is fixedly connected with the lower end of speedup fan room (7-7-12-6), and oxygen adds
Fast room (7-7-12-5) connect with the upper end of surge chamber (7-7-12-4), lower end and the oxygen spray pipe of surge chamber (7-7-12-4)
The upper end of (7-7-12-3) is fixedly connected;The internal diameter of oxygen spray pipe (7-7-12-3) is less than the interior of surge chamber (7-7-12-4)
Diameter;The junction of oxygen accelerating chamber (7-7-12-5) and surge chamber (7-7-12-4) is provided with air door (7-7-12-12), is arranged
It is connected in external air damper controller (7-7-12-9) and air door (7-7-12-12) control;It is internal in surge chamber (7-7-12-4)
Equipped with wind speed inductor (7-7-12-10);The surface of oxygen spray pipe (7-7-12-3) is provided with a large amount of through-holes;Disperse in oxygen
The upper end of mouth shell is provided with multiple acetylene flow-disturbings hole (7-7-12-1);
The igniter (7-7-2) promotes driving motor, air damper controller (7-7-12-9), wind speed inductor (7-7-12-
10), cutting temperature sensor, X-axis servo motor (5-1), Y-axis servo motor (6-1), Z axis servo motor (7-1) and water pump are equal
It is connect with controller (8).
2. a kind of residents in rural community processing equipment with oxygen dispersion mouth according to claim 1, which is characterized in that
It is solid cylinder that the oxygen, which accelerates rotation cardan shaft (7-7-12-7),.
3. a kind of residents in rural community processing equipment with oxygen dispersion mouth according to claim 1 or 2, feature exist
In the cutting nozzle shell (7-7-10) is internal to be fixedly connected with interior cover body (7-7-11), interior cover body (7-7-11) and cutting nozzle
Tempering channel (7-7-4) is formed between shell (7-7-10), the lower end of tempering channel (7-7-4) is connected to flame jet (7-7-1),
The upper end of channel (7-7-4) is tempered by being tempered valve (7-7-7) with fixing sleeve loaded on the external heat exchange of acetylene hose (7-7-9)
The entrance of device (7-7-6) connects, and the outlet of heat exchanger (7-7-6) extends to cutting nozzle shell (7-7-10) outside.
4. a kind of residents in rural community processing equipment with oxygen dispersion mouth according to claim 3, which is characterized in that
The left and right ends of the X-axis sliding rail (5-6) are both provided with moves the matched X-axis row in the left and right ends sliding block (5-7) with X-axis
Journey is to bit detector;The left and right ends of the Y-axis sliding rail (6-6) are both provided with moves the left and right ends sliding block (6-7) with Y-axis
Matched Y-axis Overstroke detector;It is equipped in the Y-axis gear mounting bracket (6-9) for detecting Y-axis driving gear
The speed probe of (6-3) rotating speed;The opposite side of the top plate (7-4) and bottom plate (7-9) is mounted on upper with sliding pair
The lower matched Z axis Overstroke detector in both ends;The X-axis Overstroke detector, Y-axis Overstroke detector, rotating speed
Sensor and Z axis Overstroke detector are connect with controller (8).
5. a kind of residents in rural community processing equipment with oxygen dispersion mouth according to claim 4, which is characterized in that
The outer side covering on cutting nozzle shell (7-7-10) top has insulating layer (7-7-5).
6. a kind of residents in rural community processing equipment and its work side with oxygen dispersion mouth according to claim 5
Method, which is characterized in that support frame as described above (1) has four supporting legs, the bottom of every supporting leg be both provided with it is height-adjustable can
Angle modulation seat.
7. a kind of residents in rural community processing equipment with oxygen dispersion mouth according to claim 6, which is characterized in that
Support frame as described above (1) is formed by stainless steel tube welding production, and the thickness of stainless steel tube is 5cm~8cm;The X-axis sliding rail
(5-6) material is nickel-clad steel plate, and thickness is 1cm~3cm;Y-axis sliding rail (6-6) material is nickel-clad steel plate, thick
Degree is 1cm~3cm;The distance between the reject chute (3) and workbench (4) are 10cm~15cm;Flame jet (the 7-7-
1) it is in truncated conical shape;The mixing chamber (7-7-3) is in coniform.
8. a kind of residents in rural community processing equipment with oxygen dispersion mouth according to claim 7, which is characterized in that
The insulating layer (7-7-5) is made of high molecular material.
9. a kind of residents in rural community processing equipment with oxygen dispersion mouth according to claim 8, which is characterized in that
The oxygen spray pipe (7-7-12-3) is composed of the following components by ratio of weight and the number of copies:
338.7~563.8 parts of purified water, 2- methyl-pentadecanoic acid -2- ethyls -2- [[(2- methyl-1s-oxo pentadecyl) oxygen]
Methyl generation] 130.6~172.4 parts of 1,3- propylidene ester, 4- methoxyl groups-α-[[methyl sulphonyl] oxygroup] imino group]-phenyl second
133.8~242.9 parts of nitrile, 3- (methyl mercapto) -129.8~146.3 parts of butyraldehyde, 132.1~189.2 parts of everbright red toner C, (1- methyl
Ethylidene) bis- (4,1- phenoxy group -2,1- ethylidene) 135.3~196.7 parts of diacetates, molybdenum nanoparticle 137.4~192.3
Part, 130.0~172.0 parts of the polymer of newtrex and alpha -hydro-omega -hydroxypoly (oxidation -1,2- second diyl), formaldehyde and [4-
The complex compound of (1,1- dimethyl ethyl) phenol and magnesia] 132.0~172.4 parts of polymer, alkali formula aluminium hydroxyacetate 132.3
~155.9 parts, 121.5~157.0 parts of the polymethylene polyphenylene isocyanates of methyl ethyl ketoxime sealing end, 2 methyl octylaldehyde
120.3~163.4 parts, 129.5~174.1 parts of formic acid -4- cyclo-octene -1- alcohol esters, 139.8~183.6 parts of polyurethane elastomer,
Mass concentration is 162.5~216.4 parts of the hexadecanyl phosphate fatting agent of 129ppm~396ppm.
10. a kind of residents in rural community processing equipment with oxygen dispersion mouth according to claim 9, feature exist
In the production method of the oxygen spray pipe (7-7-12-3) is as follows:
S1:In energy-saving type stirred reactor, purified water and 2- methyl-pentadecanoic acid -2- ethyls -2- [[(2- methyl-1s-oxygen is added
For pentadecyl) oxygen] methyl generation] 1,3- propylidene esters, start the blender in energy-saving type stirred reactor, setting speed is
131rpm~177rpm;Start energy-saving type stirred reactor in steam coil heater, make temperature rise to 146.7 DEG C~
147.8 DEG C, 4- methoxyl groups-α-[[methyl sulphonyl] oxygroup] imino group is added]-phenylacetonitrile stirs evenly, organic matter is made
Ⅰ;
S2:It is 122.7m that organic matter made from S1 I, which is passed through flow,3/ min~163.3m3123.6~134.4 points of the xenon of/min
Clock;The pH value for adjusting solution in energy-saving type stirred reactor is 4.1~8.2, keeps the temperature 123.1~363.1 minutes;Filtering, removal
Impurity obtains suspension;
S3:The poly- of formaldehyde and [complex compound of 4- (1,1- dimethyl ethyls) phenol and magnesia] is added in suspension made from S2
Object is closed, adjustment pH value forms sediment purifying water elution between 1.5~2.0;Solid content, high temperature are obtained by centrifuge
It is dry, 0.882 × 10 is crossed after grinding3Mesh sieves;Obtain the mixture of character change;
S4:The mixture that character made from S3 is changed adds to the methyl ethyl ketoxime that mass concentration is 133ppm~363ppm and blocks
Polymethylene polyphenylene isocyanates in;Start the steam coil heater in energy-saving type stirred reactor, setting is energy saving
Formula stirred reactor operating parameter is:Temperature is 207.8 DEG C~263.3 DEG C;PH is adjusted between 4.1~8.1;Pressure is
1.29MPa~1.3MPa;Reaction time is 0.4~0.9 hour;After reaction, it is depressurized to zero gauge pressure, is discharged into molding press,
Obtain oxygen spray pipe (7-7-12-3).
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