CN106622073A - Waste gas purifying and weighing integrated reaction kettle device - Google Patents

Waste gas purifying and weighing integrated reaction kettle device Download PDF

Info

Publication number
CN106622073A
CN106622073A CN201611101539.1A CN201611101539A CN106622073A CN 106622073 A CN106622073 A CN 106622073A CN 201611101539 A CN201611101539 A CN 201611101539A CN 106622073 A CN106622073 A CN 106622073A
Authority
CN
China
Prior art keywords
kettle
waste gas
linkage section
gas purification
reaction kettle
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
CN201611101539.1A
Other languages
Chinese (zh)
Inventor
张中杰
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.)
Yasusa Chemical Co Ltd
Original Assignee
Yasusa Chemical 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.)
Filing date
Publication date
Application filed by Yasusa Chemical Co Ltd filed Critical Yasusa Chemical Co Ltd
Priority to CN201611101539.1A priority Critical patent/CN106622073A/en
Publication of CN106622073A publication Critical patent/CN106622073A/en
Pending legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/18Stationary reactors having moving elements inside
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D46/00Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
    • B01D46/10Particle separators, e.g. dust precipitators, using filter plates, sheets or pads having plane surfaces
    • 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
    • B01D53/02Separation 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 by adsorption, e.g. preparative gas chromatography
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/0006Controlling or regulating processes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/0006Controlling or regulating processes
    • B01J19/0013Controlling the temperature of the process
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/0053Details of 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
    • B01J4/00Feed or outlet devices; Feed or outlet control devices
    • B01J4/008Feed or outlet control devices
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J4/00Feed or outlet devices; Feed or outlet control devices
    • B01J4/02Feed or outlet devices; Feed or outlet control devices for feeding measured, i.e. prescribed quantities of reagents
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2204/00Aspects relating to feed or outlet devices; Regulating devices for feed or outlet devices
    • B01J2204/002Aspects relating to feed or outlet devices; Regulating devices for feed or outlet devices the feeding side being of particular interest
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00049Controlling or regulating processes
    • B01J2219/00051Controlling the temperature
    • B01J2219/00074Controlling the temperature by indirect heating or cooling employing heat exchange fluids
    • B01J2219/00076Controlling the temperature by indirect heating or cooling employing heat exchange fluids with heat exchange elements inside the reactor
    • B01J2219/00081Tubes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/18Details relating to the spatial orientation of the reactor
    • B01J2219/185Details relating to the spatial orientation of the reactor vertical

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Analytical Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Processing Of Solid Wastes (AREA)

Abstract

The invention relates to a waste gas purifying and weighing integrated reaction kettle device which comprises a kettle body, a waste gas treating and purifying device and a weighing device arranged at the top of the kettle body. A kettle cover is arranged at the top of the kettle body, a material inlet, a gas discharging hole and a thermometer sleeve are arranged on the kettle cover, and the waste gas treating and purifying device is positioned at the upper end of the kettle body and fixed through a mounting frame. By arranging a waste gas filtering layer, a waste gas adsorbing layer and a waste gas ventilating layer, a lot of high-concentration organic waste gas generated in the process of reaction for preparing adhesive resin can be treated and absorbed to reach discharging standards; a ventilating wall plate having a certain inclination angle is arranged, so that noise in the process when a fan runs can be lowered. The waste gas purifying and weighing integrated reaction kettle device is compact in structure, high in automation level and convenient and simple to operate.

Description

It is a kind of to weigh integral type reaction kettle device for waste gas purification
Technical field
The invention belongs to resin processing equipment technical field, and in particular to a kind of to weigh integral type reaction for waste gas purification Kettle device.
Background technology
Reactor is widely used in oil, chemical industry, rubber, agricultural chemicals, dyestuff, medicine, food, for completing to vulcanize, nitrifying, The pressure vessel of the technical process such as hydrogenation, hydrocarbonylation, polymerization, condensation, such as reactor, reaction pot, decomposition pot, polymeric kettle etc.;Material Matter typically has carbon manganese steel, stainless steel, zirconium, Ni-based(Kazakhstan, Monel, inconel)Alloy and other composites.Reactor Broad understanding has the rustless steel container for physically or chemically reacting, and is set according to the structure that different process conditions demands carries out container Meter and parameter configuration, design condition, process, inspection and manufacture, examination are needed according to Its Relevant Technology Standards, to realize technological requirement The mixture response function of heating, evaporation, cooling and low high speed.
Adhesive agent is also referred to as adhesive, binder, in 1742 by American Henry Al Kut doctors(Dr. Harry Coover)Invention.Refer to by the glutinous material together of two objects, according to the characteristic of wanted bonding material(Mainly surface characteristic, Such as roughness), using different adhesive agents;Binder is in fact the resin of dilution, and resin inherently has stickiness.
Reactor is conventional chemical industry equipment;During reaction prepares adhesive, it will usually produce substantial amounts of high concentration Organic exhaust gas, this aspect derives from the gas-phase product of synthetic reaction, on the other hand from the volatilization for reacting solvent after heating. Because synthetic reaction generally will be heated, or exothermic reaction produces heat, raises the temperature of charge in reactor, so as to Significantly increase the organic concentration in reactor top gas phase.
Generally, reactor top is provided with blast pipe, and waste gas is discharged into reactor.Cause to prevent reactor from discharging waste gas Atmosphere pollution, by blast pipe discharge waste gas lead to exhaust treatment system process it is qualified after could discharge.Existing one kind Technical scheme, in the top of exhaust outlet gas skirt is installed, and gas skirt is connected with collecting pipe, and waste gas is sent to into exhaust-gas treatment System.The deficiency of this technical scheme is, when the negative pressure of gas skirt it is not enough, or blast pipe discharge the flow or pressure of waste gas compared with When big, waste gas can not all collected by gas skirt, and a part of waste gas can be directly diffused in air and form pollution.It is existing another A kind of technical scheme, is that blast pipe is directly connected to into collecting pipe, it is possible to guarantee that the waste gas that blast pipe is discharged is fully entered Exhaust treatment system process.The deficiency of this scheme is, in order to realize discharging in a organized way, collecting pipe needs to be born with certain Pressure, directly connect with blast pipe carries out negative-pressure ward equivalent to reactor, significantly increases the discharge capacity of reactor waste gas.This The load of emission-control equipment is not only increased, and causes the waste of organic solvent;Meanwhile, reactor fan and gas collection Noise problem produced by pipeline can directly affect in such an environment for a long time the healthy of worker than larger.
In addition, the material thrown in into reactor is typically first placed on electronic scale and weighs, then entering by reactor Material mouth is put into kettle, the mode of such manual control charging, the weight of the difficult accurate control feed liquid of comparison, application condition Greatly;Also to ensure that the feeding port for throwing in material is accurately docked with the charging aperture of reactor simultaneously, once docking is inaccurate, can spill into Product material, causes the loss of material, if material is poisonous or inflammable and explosive material, the generation for easily causing the accident, and And existing reactor single function, inefficiency, mixing effect are poor, it is impossible to meet the demand of modernization Chemical Manufacture.
For above-mentioned technical problem, therefore need to be improved.
The content of the invention
The present invention is to overcome above-mentioned defect of the prior art, there is provided a kind of anti-for waste gas purification integral type of weighing Kettle device is answered, the device can carry out purified treatment during reactor prepares adhesive agent to waste gas, it is also possible to reduce noise dirty Dye, meanwhile, precise control weight can be carried out to the material for adding, it is ensured that the qualification rate of adhesive agent product, the apparatus structure is simple, It is easy to use.
In order to reach object above, the technical solution adopted in the present invention is:It is a kind of to weigh integral type for waste gas purification Reaction kettle device, including kettle, exhaust gas purification device and the weighing device at the top of kettle;Set at the top of the kettle There is kettle cover, kettle cover is provided with charging aperture, steam vent and thermometer boss;Exhaust gas purification device is located at the upper end of kettle and leads to Cross installing rack to fix;The bottom of exhaust gas purification device is provided with the first connecting tube in trumpet type, the first connection bottom of the tube It is connected with steam vent;The thermometer boss is stretched in kettle and upper end is fixed on the kettle cover, the thermometer boss Thermometer is inside set, autoclave body bottom is provided with discharging opening;Agitating device is provided with kettle;The bottom of kettle is arranged installs bracing frame;Institute Weighing device is stated including storage bin;The lower end of storage bin is provided with two discharging openings of tapered cavity;Storage bin lower end is provided with The LOAD CELLS corresponding with discharging opening, is provided with connected terminal box by LOAD CELLS;Terminal box is installed on title Retransmit on the side wall of sensor, the centre position of two discharging openings extends vertically be provided with deflector upwards, deflector is located at storage bin Interior, the height of deflector is the 1/2 of storage bin height, and the upper port of storage bin is provided with material inlet valve, corresponding, goes out The lower port of material mouth is provided with discharge gate, and discharge gate bottom is connected with buffering filtering chamber, buffers the bottom of filtering chamber The flexible discharger slip awaing tube of connection one, the lower end connection reducing mechanism of flexible discharger slip awaing tube;The reducing mechanism includes screw feeding Machine, screw feeding motor spindle is provided with connecting tube, and the bottom of self-conveyor feed is also equipped with Weighing mechanism and self-conveyor feed On be provided with motor, self-conveyor feed is connected by connecting tube with Weighing mechanism;The Weighing mechanism includes being installed on connecting tube On weight sensor and material tremie pipe;Material tremie pipe is connected with the charging aperture on kettle;The upper end peace of material tremie pipe Equipped with material blanking control valve door;Weight sensor is connected with material blanking control valve door;The agitating device includes driving Motor, bracing frame, shaft and stirring paddle mechanism;Bracing frame is fixedly arranged on kettle cover, and motor is located on bracing frame, shaft One end and motor rotate and be connected, the other end is passed through in kettle and stirs paddle mechanism and be connected;The exhaust-gas treatment purification dress Put including housing, the waste gas filter layer laid successively from the bottom to top in housing, waste gas adsorption layer and waste air ventilation layer;Waste gas Filter layer, between waste gas adsorption layer and waste air ventilation layer gap is respectively kept with;The waste gas filter layer is labyrinth type filter layer, should Labyrinth type filter layer is waveform bilayer paper structure, and before and after the duplex paper perforate is intersected;Waste gas adsorption layer is activated carbon filter layer, Activated carbon is filled with activated carbon filter layer.
Used as a preferred embodiment of the present invention, the waste air ventilation layer includes being located in housing leading to certain knuckle Wind passage;The vent passages are formed by connecting by least two pieces identicals ventilation wallboards;Vent passages lower end is connected with for fixing The reinforcement of ventilation wallboard.
Used as a preferred embodiment of the present invention, the ventilation wallboard is connected by the first linkage section, the second linkage section and the 3rd Connect section to be formed by fixedly connecting, be integrally formed;First linkage section is vertical with the top of housing to be connected, and the 3rd linkage section hangs down with reinforcement Direct-connected to connect, the second linkage section is oblique, for connecting the first linkage section and the 3rd linkage section.
As the equal length of a preferred embodiment of the present invention, second linkage section and the 3rd linkage section;First connects The length for connecing section is the 1/2 of the 3rd connection segment length;Second linkage section and the first linkage section and the 3rd linkage section in 25 °~ 65 ° of angle is inclined.
Used as a preferred embodiment of the present invention, the case top is provided with discharge duct, and discharge duct lower end is installed There is trumpet type suction opeing, trumpet type suction opeing upper end is provided with air exhauster.
As a preferred embodiment of the present invention, on the kettle body sidewall steam inlet and steam (vapor) outlet are separately installed with; Steam pipe is connected between steam inlet and steam (vapor) outlet, steam pipe annular is laid in the inwall of kettle, the steam pipe with stirring Paddle mechanism keeps certain spacing.
Used as a preferred embodiment of the present invention, the stirring paddle mechanism includes from top to bottom being laid in successively on shaft Hinging type stirrer paddle, pusher blade and four leaf swept-back blades;After hinging type stirrer paddle, pusher blade and four leaves The formula blade of plunderring is socketed on shaft, is removable connection with shaft;The hinging type stirrer paddle, pusher blade and four Leaf swept-back blade is equidistantly laid on shaft;The blade tip of the four leaves swept-back blade is in sharp portion.
Used as a preferred embodiment of the present invention, the kettle cover has the pressure sensor under extending to the cavity of kettle, Pressure sensor connects temperature and pressure device for digit-displaying, and by temperature and pressure device for digit-displaying the pressure in kettle is shown.
As a preferred embodiment of the present invention, PLC control system is also included, the PLC control system and weighing and sensing The electrical connection of device, terminal box and weight sensor.
Used as a preferred embodiment of the present invention, the material inlet valve, discharge gate adopt air cylinder driven, material inlet valve Also carry hand door.
The invention has the beneficial effects as follows:
1. one kind that the present invention is provided is weighed integral type reaction kettle device for waste gas purification, and there is the device precise control to feed The function of speed, reduces the artificial danger that material is directly put into reactor, reduces the labour intensity of operator, improves Execute-in-place environment, improves the security of reaction unit;Connected using steam inlet, steam (vapor) outlet and steam pipe so that The heat exchange efficiency of reactor is greatly improved, and heat exchange response speed greatly speeds up;It is sealing in the operating process of liquid material, Material reaches environmental pollution and the wasting of resources for avoiding that Chang Kou Installed material strips come in reactor container from storage tank Jing delivery pumps;
2. it is comprehensive by using hinging type stirrer paddle, pusher blade and four three kinds of different stirrer paddles of leaf swept-back blade Conjunction make use of the advantage of three kinds of blades, had both changed and has mixed that uneven, polymerization efficiency is low to ask present in traditional agitating mode Topic, causes reaction stability to significantly improve again;
3. PLC control system realize the typing of the Weighing process data of the material of whole reaction kettle device, collection, contrast, The functions such as quantitative control, and can be communicated with computer control system by data-interface, realize intelligentized control method;
4. by arranging waste gas filter layer, waste gas adsorption layer and waste air ventilation layer, can be to preparing adhesive resin mistake in reaction Substantial amounts of high-concentration organic waste gas are produced in journey to be processed, is absorbed, reach discharge standard, while arrange that there is certain inclination angle The ventilation wallboard of degree, can reduce noise during fan operation, and the apparatus structure is compact, high degree of automation, operation side Just it is simple;
5. the present invention has integrated level high, and high degree of automation is user-friendly for operation, easy to maintenance simple, quantitatively accurately, environmental protection etc. Feature, with good application value.
Description of the drawings
Fig. 1 is embodiment of the present invention structural representation;
Reference in figure:Installing rack 1, housing 2, waste gas filter layer 3, waste gas adsorption layer 4, waste air ventilation layer 5, vent passages 6, Ventilation wallboard 7, the first linkage section 7-1, the second linkage section 7-2, the 3rd linkage section 7-3, storage bin 8, discharging opening 9, deflector 10, Kettle 11, charging aperture 12, discharging opening 13 installs bracing frame 14, kettle cover 15, steam vent 16, reinforcement 17, discharge duct 18, loudspeaker Type suction opeing 19, LOAD CELLS 20, terminal box 21, discharge gate 22, flexible discharger slip awaing tube 23, material inlet valve 24, buffering Filtering chamber 25, self-conveyor feed 26, motor 27, connecting tube 28, Weighing mechanism 29, weight sensor 29-1, material tremie pipe 29-2, blanking control valve door 29-3, motor 30, bracing frame 31, shaft 32, steam inlet 33, steam (vapor) outlet 34, steam Pipe 35, hinging type stirrer paddle 36, pusher blade 37, four leaf swept-back blades 38, pressure sensor 39, pressure device for digit-displaying 40, thermometer boss 41, air exhauster 42, the first connecting tube 43.
Specific embodiment
The embodiment of the present invention is elaborated below in conjunction with the accompanying drawings.
Embodiment 1:It is as shown in figure 1, one kind is weighed integral type reaction kettle device for waste gas purification including kettle 11, useless Gas disposal purifier and the weighing device located at the top of kettle 11;The top of the kettle 11 is provided with kettle cover 15, on kettle cover 15 It is provided with charging aperture 12, steam vent 16 and thermometer boss 41;Exhaust gas purification device is located at the upper end of kettle 11 and by peace Shelve 1 fixation;The bottom of exhaust gas purification device is provided with the first connecting tube 43 in trumpet type, the bottom of the first connecting tube 43 It is connected with steam vent 16;By arranging exhaust gas purification device, using the first connecting tube, 43 pairs prepare adhesive in reaction Substantial amounts of high-concentration organic waste gas are produced in resin process to be processed, is absorbed, reach discharge standard, can greatly mitigate environment Pollution, protects well that employee's is healthy.
Thermometer boss 41 is stretched in kettle 11 and upper end is fixed on the kettle cover 15, sets in the thermometer boss 41 Thermometer, thermometer can at any time show the temperature in kettle 11, and to using bringing convenience, the bottom of kettle 11 is provided with discharging opening 13; Agitating device is provided with kettle 11;The bottom of kettle 11 is arranged installs bracing frame 14, installs bracing frame 14 and causes the reactor dress The stability put is more preferable, using safer.
Weighing device includes storage bin 8;The lower end of storage bin 8 is provided with two discharging openings 9 of tapered cavity;Storage bin 8 lower ends are provided with the LOAD CELLS 20 corresponding with discharging opening 9, and connected terminal box is provided with by LOAD CELLS 20 21;Terminal box 21 is installed on the side wall of LOAD CELLS 20, and the centre position of two discharging openings 9 extends vertically to be provided with upwards leads Stream plate 10, deflector 10 is located in storage bin 8, and the height of deflector 10 is the 1/2 of the height of storage bin 8, what deflector 10 was arranged Purpose is to make 24 mouthfuls of materials for falling of each material inlet valve, uniformly by two discharging openings 9 of the corresponding tapered cavity in its lower end Flow out, it is ensured that inventory is balanced on each discharging opening 9, realizes uniform blanking, reduces the stability of the solid weighing device.
The upper port of storage bin 8 is provided with material inlet valve 24, corresponding, and the lower port of discharging opening 9 is provided with unloads Material valve 22, the bottom of discharge gate 22 is connected with buffering filtering chamber 25, and the bottom for buffering filtering chamber 25 connects a flexibility Discharger slip awaing tube 23, the lower end connection reducing mechanism of flexible discharger slip awaing tube 23;The position of flexible discharger slip awaing tube 23 is arranged, and makes buffered Filter chamber room 25 be capable of the lifting of flexible discharger slip awaing tube 23 and lift, the solid that moves left and right and move to meet differing heights claims Refitting is put, and can make have as little as possible between the port of material tremie pipe 29-2 and the upper surface of charging aperture 12 of kettle 11 as far as possible Distance is reducing flour dust overflow;The LOAD CELLS 20 corresponding with discharging opening 9, weighing and sensing are set at the position of discharging opening 9 Device 20 is electrically connected with terminal box 21, for detecting storage bin 8 in material weights.
Reducing mechanism includes self-conveyor feed 26, and the bottom of self-conveyor feed 26 is provided with connecting tube 28, self-conveyor feed 26 Bottom be also equipped with being provided with motor 27 on Weighing mechanism 29 and self-conveyor feed 26, self-conveyor feed 26 pass through connecting tube 28 are connected with Weighing mechanism 29;Weighing mechanism 29 includes the weight sensor 29-1 and material tremie pipe being installed in connecting tube 28 29-2;Material tremie pipe 29-2 is connected with the charging aperture 12 on kettle 11;The upper end of material tremie pipe 29-2 is provided with material Material control valve 29-3;Weight sensor 29-1's is connected with material blanking control valve door 29-3;By self-conveyor feed 26 pairs The stirring and processing of material, according to actual needs, the charging frequency of adjustable screw charger 26 drives screw feeding by motor 27 Machine 26 rotates, and the material for processing enters to Weighing mechanism 29 by connecting tube 28, and by Weighing mechanism 29 quantifying feed is realized Purpose, the apparatus structure is simple, and reasonable in design, detachability is good, is easily installed and changes, and fault rate is low, stability in use Good, the device has the function of precise control charging rate, reduces the artificial danger that solid material is directly put into kettle 11 Property, the labour intensity of operator is reduced, execute-in-place environment is improved, improve the security of reaction unit.
Material inlet valve 24, discharge gate 22 adopt air cylinder driven, material inlet valve 24 also to carry hand door, facilitate user Debugging, maintenance.Dust explosion protection type proximity switch is filled on material inlet valve 24, the detection and control of the bin gate position of material inlet valve 24 is carried out System, it is ensured that the security that material is added.
The agitating device includes motor 30, bracing frame 31, shaft 32 and stirring paddle mechanism;Bracing frame 31 is fixed On kettle cover 15, motor 30 is located on bracing frame 31, and one end of shaft 32 rotates with motor 30 and is connected, the other end It is passed through in kettle 11 and is connected with stirring paddle mechanism.
Exhaust gas purification device includes housing 2, the waste gas filter layer 3 laid successively from the bottom to top in housing 2, gives up Gas adsorption layer 4 and waste air ventilation layer 5;Waste gas filter layer 3, between waste gas adsorption layer 4 and waste air ventilation layer 5 gap is respectively kept with; Waste gas filter layer 3 is labyrinth type filter layer, and the labyrinth type filter layer is waveform bilayer paper structure, intersects before and after the duplex paper and opens Hole;Waste gas adsorption layer 4 is that activated carbon is filled with activated carbon filter layer, activated carbon filter layer.
The labyrinth type filter layer is waveform bilayer paper structure, and before and after the duplex paper perforate is intersected;Labyrinth type filter layer is adopted Made with ground paper, particular/special requirement is had no to the ground paper that labyrinth type filter layer is adopted, corrugated paper can be adopted, in agitating device to kettle The adhesive resin raw material for preparing in 11 is stirred, and waste gas passes through the connecting tube 43 of steam vent 16 and first when housing 2, Under the operation of air exhauster 42, when labyrinth type filter layer, the particulate matter contained by the inside can be because used for the pernicious gas in waste gas Property and cyclogenesis adhere on labyrinth type filter layer, meanwhile, for the ease of clear up labyrinth type filter layer on filtration particle, give up Gas filter layer 3 is to be detachably connected with housing 2;Waste gas adsorption layer 4 is filled with work in activated carbon filter layer, activated carbon filter layer Property charcoal;Waste gas impurity after waste gas filter layer 3 is filtered, by the air draught of air exhauster 42 so that waste gas impurity is by property charcoal The activated carbon of filter layer is adsorbed, effectively to remove removing exhaust gas impurity in waste organic solvent gas, finally, tail gas up to standard by row Feed channel 18 is entered in air.
Waste air ventilation layer 5 includes being located at the vent passages 6 with certain knuckle in housing 2;The vent passages 6 are by least two Block identical ventilation wallboard 7 is formed by connecting;The lower end of vent passages 6 is connected with for the reinforcement 22 of fixed ventilation wallboard 7;Using Vent passages 6 cause air exhauster 25 in running, effectively reduce the interference of noise.
Ventilation wallboard 7 is formed by fixedly connecting by the first linkage section 7-1, the second linkage section 7-2 and the 3rd linkage section 7-3, and one It is body formed;First linkage section 7-1 is vertical with the top of housing 2 to be connected, and the 3rd linkage section 7-3 is vertical with reinforcement 22 to be connected, the Two linkage section 7-2 are oblique, for connecting the first linkage section 7-1 and the 3rd linkage section 7-3.
Using such scheme so that in operation, the wind direction for being absorbed runs from the bottom to top air exhauster 25, the adjacent the 3rd The vent passages 6 that linkage section 7-3 is formed are vertical direction, in motion process on wind direction, because the second linkage section 7-2 is in incline Ramp-like setting, the wind of upward vertical movement can touch the second linkage section 7-2, produce wind direction skew, give wind direction certain stagnant Use is given over to, while so that wind speed is reduced, and then reduction blower fan moves brought noise.
Optimize for the ease of the height of the waste air ventilation layer 5 so that the structure of emission-control equipment is more convenient and utilizes Rate is high, the equal length of the second linkage section 7-2 and the 3rd linkage section 7-3;The length of the first linkage section 7-1 is the 3rd linkage section 7- The 1/2 of 3 length;While ensureing to reduce noise, and ventilation efficiency can be caused higher.
Second linkage section 7-2 and the first linkage section 7-1 and the 3rd linkage section 7-3 is inclined in 25 °~35 ° of angle;This dress The the second linkage section 7-2 for putting is 50 ° of inclinations, and the effect for reducing noise is more preferable.
Steam inlet 33 and steam (vapor) outlet 34 are separately installed with the side wall of kettle 11;Steam inlet 33 and steam (vapor) outlet 34 it Between be connected with steam pipe 35, the annular of steam pipe 35 is laid in the inwall of kettle 11, the steam pipe 35 with stirring paddle mechanism keep one Fixed spacing;In can realizing stirring paddle mechanism to adhesive resin material whipping process using such scheme, add while stirring Heat so that the adhesive resin material of stirring is heated evenly, the reaction time of material accelerates, and makes reaction more abundant, improves Mixing effect and stirring efficiency of the adhesive resin material in kettle 11, this apparatus structure is simple, easy to use.
Stirring paddle mechanism includes the hinging type stirrer paddle 36, push-paddle being from top to bottom laid in successively on shaft 32 The leaf swept-back blade 38 of leaf 37 and four;By arranging three kinds of different stirrer paddles, stirring efficiency and mixing quality are made all significantly Improve, bring great convenience to agitating procedure so that stirring efficiency is effectively improved, improve mixing quality;Meanwhile, Hinging type stirrer paddle 36, the pusher leaf swept-back blade 38 of blade 37 and four are set, are so arranged in whipping process and are subject to Resistance it is less, while good action of turbulent flow can be carried out to material web so that stirring is more uniform.
Hinging type stirrer paddle 36, the pusher leaf swept-back blade 38 of blade 37 and four are socketed on shaft 32, and are stirred Mix the removable connection of axle 32;It is easy to hinging type stirrer paddle 36, the maintenance of the pusher leaf swept-back blade 38 of blade 37 and four, energy Enough conveniently fast disassemblings are changed, and cleaning is easy, and can change different stirring paddle mechanisms according to process condition, are realized optimal Mixing effect, use range is wide, and service efficiency is high.
Hinging type stirrer paddle 36, the pusher leaf swept-back blade 38 of blade 37 and four are equidistantly laid on shaft 32, So that stirring is more uniform so that stirring efficiency is effectively improved, and improves mixing quality.
Because four leaf swept-back blades 38 are located at the bottommost of reactor, material is thrown in from charging aperture 12 to reactor During, pass sequentially through hinging type stirrer paddle 36, the stirring of the pusher leaf swept-back blade 38 of blade 37 and four so that material Stirring it is more uniform, meanwhile, the blade tip of four leaf swept-back blades 38 is in sharp portion, further increases cutting for material Cut efficiency and cutting utilization rate.
Also just because of the blade tip of four leaf swept-back blade 38 is in sharp portion so that front shear force is larger, it is sufficient to make monomer Material be separated into fine droplets and can uniformly be suspended in liquid phase, be easy to polymerization and will not agglomeration pile up it is blocking;The stream circulation of stirring liquid is special Property it is good, liquid can be made to produce simultaneously and axially and radially to be moved;So that liquid carries out sufficiently circulation to eliminate the uneven of temperature Property, heat-transfer effect is good, and discharge rate is big;Liquid phase circulation is per minute good up to 5~10 mass transfer effects in kettle, and reaction in kettle can be made equal It is even consistent;Adapt to the change of proportion during vinylite preparation manipulation;Can with one layer of stirrer paddle replace several layers other The paddle of pattern, makes to simplify the structure easy to maintenance.
By using hinging type stirrer paddle 36, pusher blade 37 and four 38 3 kinds of different stirrings of leaf swept-back blade Blade, fully utilizes the advantage of three kinds of blades, has both changed and has mixed uneven, polymerization efficiency present in traditional agitating mode Low problem, causes reaction stability to significantly improve again;In order to increase service life and using effect, hinging type paddle Leaf 36, the pusher leaf swept-back blade 38 of blade 37 and four are propeller agitator, hinging type stirrer paddle 36, push-paddle The leaf swept-back blade 38 of leaf 37 and four is solid forging and forms, and stress is more concentrated, not easy fracture.
Kettle cover 15 has the pressure sensor 39 under extending to, the connection temperature of pressure sensor 39 and pressure to the cavity of kettle 11 Power device for digit-displaying 40, shows the pressure in kettle 11, it is ensured that the safety in utilization of reactor by temperature and pressure device for digit-displaying 40.
A kind of waste gas purification apparatus of multifunctional reaction still, also includes PLC control system, the PLC control system with claim Retransmit sensor 20, terminal box 21 and weight sensor 29-1 electrical connection;By LOAD CELLS 20 and weight sensor 29-1 point The weight of material is weighed respectively after other material and smashing to adding, the PLC control system control for then passing the result to System, PLC control system is adjusted according to pre-setting, meanwhile, warning function is additionally provided with PLC control system control, make work Make spilling or deficiency that personnel know in time material, increase the service life of equipment.
The foregoing description of the disclosed embodiments, enables professional and technical personnel in the field to realize or using the present invention. Various modifications to these embodiments will be apparent for those skilled in the art, as defined herein General Principle can be realized in other embodiments without departing from the spirit or scope of the present invention;Therefore, the present invention The embodiments shown herein is not intended to be limited to, and is to fit to and principles disclosed herein and features of novelty phase one The most wide scope for causing.
Although more having used reference in figure herein:Installing rack 1, housing 2, waste gas filter layer 3, waste gas adsorption layer 4, waste air ventilation layer 5, vent passages 6, wallboard 7 of divulging information, the first linkage section 7-1, the second linkage section 7-2, the 3rd linkage section 7-3, Storage bin 8, discharging opening 9, deflector 10, kettle 11, charging aperture 12, discharging opening 13 installs bracing frame 14, kettle cover 15, steam vent 16, reinforcement 17, discharge duct 18, trumpet type suction opeing 19, LOAD CELLS 20, terminal box 21, discharge gate 22, flexibility is unloaded Material elephant trunk 23, material inlet valve 24 buffers filtering chamber 25, self-conveyor feed 26, motor 27, connecting tube 28, Weighing mechanism 29, weight Quantity sensor 29-1, material tremie pipe 29-2, blanking control valve door 29-3, motor 30, bracing frame 31, shaft 32 steams Vapor inlet 33, steam (vapor) outlet 34, steam pipe 35, hinging type stirrer paddle 36, pusher blade 37, four leaf swept-back blades 38, Pressure sensor 39, pressure device for digit-displaying 40, thermometer boss 41, the grade term of air exhauster 42, but be not precluded from using other terms Possibility.It is used for the purpose of more easily describing and explaining the essence of the present invention using these terms;It is construed as appointing A kind of what additional restriction is all contrary with spirit of the invention.

Claims (10)

1. one kind for waste gas purification weigh integral type reaction kettle device, it is characterised in that:Including kettle(11), exhaust-gas treatment it is net Makeup is put and located at kettle(11)The weighing device at top;The kettle(11)Top be provided with kettle cover(15), kettle cover(15)On It is provided with charging aperture(12), steam vent(16)And thermometer boss(41);Exhaust gas purification device is located at kettle(11)Upper end And by installing rack(1)It is fixed;The bottom of exhaust gas purification device is provided with the first connecting tube in trumpet type(43), first Connecting tube(43)Bottom and steam vent(16)It is connected;The thermometer boss(41)Stretch into kettle(11)Interior and upper end is fixed on The kettle cover(15)On, the thermometer boss(41)Inside set thermometer, kettle(11)Bottom is provided with discharging opening(13);Kettle (11)Inside it is provided with agitating device;Kettle(11)Bottom arrange install bracing frame(14);The weighing device includes storage bin (8);Storage bin(8)Lower end be provided with two discharging openings of tapered cavity(9);Storage bin(8)Lower end is provided with and discharging opening (9)Corresponding LOAD CELLS(20), LOAD CELLS(20)Side is provided with connected terminal box(21);Terminal box (21)It is installed on LOAD CELLS(20)Side wall on, two discharging openings(9)Centre position extend vertically be provided with water conservancy diversion upwards Plate(10), deflector(10)Positioned at storage bin(8)It is interior, deflector(10)Height be storage bin(8)The 1/2 of height, storage bin (8)Upper port be provided with material inlet valve(24), corresponding, discharging opening(9)Lower port be provided with discharge gate (22), discharge gate(22)Bottom is connected with buffering filtering chamber(25), buffer filtering chamber(25)Bottom connect one it is soft Property discharger slip awaing tube(23), flexible discharger slip awaing tube(23)Lower end connection reducing mechanism;The reducing mechanism includes self-conveyor feed (26), self-conveyor feed(26)Bottom is provided with connecting tube(28), self-conveyor feed(26)Bottom be also equipped with Weighing mechanism (29)And self-conveyor feed(26)On be provided with motor(27), self-conveyor feed(26)By connecting tube(28)With Weighing mechanism (29)It is connected;The Weighing mechanism(29)Including being installed on connecting tube(28)On weight sensor(29-1)With material tremie pipe (29-2);Material tremie pipe(29-2)With kettle(11)On charging aperture(12)It is connected;Material tremie pipe(29-2)Upper end peace Equipped with material blanking control valve door(29-3);Weight sensor(29-1)With material blanking control valve door(29-3)Connection;Institute Agitating device is stated including motor(30), bracing frame(31), shaft(32)With stirring paddle mechanism;Bracing frame(31)It is fixedly arranged on Kettle cover(15)On, motor(30)Positioned at bracing frame(31)On, shaft(32)One end and motor(30)The company of rotation Connect, the other end is passed through kettle(11)It is interior to be connected with stirring paddle mechanism;The exhaust gas purification device includes housing(2), be located at Housing(2)The waste gas filter layer inside laid successively from the bottom to top(3), waste gas adsorption layer(4)With waste air ventilation layer(5);Waste gas mistake Filtering layer(3), waste gas adsorption layer(4)With waste air ventilation layer(5)Between be respectively kept with gap;The waste gas filter layer(3)For labyrinth Formula filter layer, the labyrinth type filter layer is waveform bilayer paper structure, and before and after the duplex paper perforate is intersected;Waste gas adsorption layer(4) To be filled with activated carbon in activated carbon filter layer, activated carbon filter layer.
It is 2. according to claim 1 a kind of to weigh integral type reaction kettle device for waste gas purification, it is characterised in that:It is described Waste air ventilation layer(5)Including positioned at housing(2)The interior vent passages with certain knuckle(6);The vent passages(6)By at least two Block identical ventilation wallboard(7)It is formed by connecting;Vent passages(6)Lower end is connected with for fixed ventilation wallboard(7)Reinforcement (17).
It is 3. according to claim 2 a kind of to weigh integral type reaction kettle device for waste gas purification, it is characterised in that:It is described Ventilation wallboard(7)By the first linkage section(7-1), the second linkage section(7-2)With the 3rd linkage section(7-3)It is formed by fixedly connecting, one It is body formed;First linkage section(7-1)With housing(2)Top vertically connect, the 3rd linkage section(7-3)With reinforcement(17)Vertically Connection, the second linkage section(7-2)Obliquely, for connecting the first linkage section(7-1)With the 3rd linkage section(7-3).
It is 4. according to claim 3 a kind of to weigh integral type reaction kettle device for waste gas purification, it is characterised in that:It is described Second linkage section(7-2)With the 3rd linkage section(7-3)Equal length;First linkage section(7-1)Length be the 3rd linkage section (7-3)The 1/2 of length;Second linkage section(7-2)With the first linkage section(7-1)With the 3rd linkage section(7-3)In 25 °~ 65 ° of angle is inclined.
It is 5. according to claim 3 a kind of to weigh integral type reaction kettle device for waste gas purification, it is characterised in that:It is described Housing(2)Top is provided with discharge duct(18), discharge duct(18)Lower end is provided with trumpet type suction opeing(19), trumpet type takes out Air port(19)Upper end is provided with air exhauster(42).
It is 6. according to claim 1 a kind of to weigh integral type reaction kettle device for waste gas purification, it is characterised in that:It is described Kettle(11)Steam inlet is separately installed with the wall of side(33)And steam (vapor) outlet(34);Steam inlet(33)And steam (vapor) outlet(34) Between be connected with steam pipe(35), steam pipe(35)Annular is laid in kettle(11)Inwall, the steam pipe(35)With paddle Mechanism keeps certain spacing.
7. the one kind according to claim 1 or 6 for waste gas purification weigh integral type reaction kettle device, it is characterised in that: The stirring paddle mechanism includes from top to bottom being laid in shaft successively(32)On hinging type stirrer paddle(36), push-paddle Leaf(37)With four leaf swept-back blades(38);Hinging type stirrer paddle(36), pusher blade(37)With four leaf swept-back blades (38)It is socketed on shaft(32)On, with shaft(32)For removable connection;The hinging type stirrer paddle(36), it is pusher Blade(37)With four leaf swept-back blades(38)Equidistantly it is laid in shaft(32)On;The four leaves swept-back blade(38)Leaf Piece end is in sharp portion.
It is 8. according to claim 1 a kind of to weigh integral type reaction kettle device for waste gas purification, it is characterised in that:It is described Kettle cover(15)To kettle(11)Cavity have pressure sensor under extending to(39), pressure sensor(39)Connection temperature and pressure Power device for digit-displaying(40), by temperature and pressure device for digit-displaying(40)Show kettle(11)Interior pressure.
It is 9. according to claim 1 a kind of to weigh integral type reaction kettle device for waste gas purification, it is characterised in that:Also wrap PLC control system is included, the PLC control system and LOAD CELLS(20), terminal box(21)And weight sensor(29-1)Electricity Connection.
It is 10. according to claim 1 a kind of to weigh integral type reaction kettle device for waste gas purification, it is characterised in that:Institute State material inlet valve(24), discharge gate(22)Adopt air cylinder driven, material inlet valve(24)Also carry hand door.
CN201611101539.1A 2016-12-05 2016-12-05 Waste gas purifying and weighing integrated reaction kettle device Pending CN106622073A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201611101539.1A CN106622073A (en) 2016-12-05 2016-12-05 Waste gas purifying and weighing integrated reaction kettle device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201611101539.1A CN106622073A (en) 2016-12-05 2016-12-05 Waste gas purifying and weighing integrated reaction kettle device

Publications (1)

Publication Number Publication Date
CN106622073A true CN106622073A (en) 2017-05-10

Family

ID=58819385

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201611101539.1A Pending CN106622073A (en) 2016-12-05 2016-12-05 Waste gas purifying and weighing integrated reaction kettle device

Country Status (1)

Country Link
CN (1) CN106622073A (en)

Cited By (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107983287A (en) * 2017-12-16 2018-05-04 河南莱帕克化工设备制造有限公司 resin polymerization pilot experiment system
CN108404815A (en) * 2018-04-12 2018-08-17 潘玉娇 A kind of polyurethane water-proof paint manufacturing and processing equipment
CN108514853A (en) * 2018-07-03 2018-09-11 台州道致科技股份有限公司 A kind of solid automatic feeding system
CN108816166A (en) * 2018-07-11 2018-11-16 协建(江苏)智能装备有限公司 A kind of chemical reaction reaction kettle of automatic Regulation
CN110109412A (en) * 2019-06-04 2019-08-09 珂黎艾(上海)环保科技有限公司 A kind of dosing control unit of vehicle tail gas emission control clarifier production
CN110975734A (en) * 2019-12-17 2020-04-10 湖州联科粘合剂有限公司 Stirring process for producing formaldehyde-free white glue
CN111604021A (en) * 2020-06-05 2020-09-01 舟山欧莱克新材料科技有限公司 Oxidation reaction system for preparing red-based KD and control method thereof
CN112791680A (en) * 2020-12-24 2021-05-14 华阳新材料科技集团有限公司 A nickel phosphorus complex synthesis system for adiponitrile production
CN113041982A (en) * 2021-03-18 2021-06-29 河南鑫利安全技术服务有限责任公司 Hazardous chemicals processing equipment with warning device
CN113137607A (en) * 2021-04-25 2021-07-20 浙江宏电环保装备有限公司 Waste gas particle treatment device and use method thereof
CN113244810A (en) * 2021-05-11 2021-08-13 陈燕利 Efficient reaction kettle for water-based ink production and production process thereof
CN113477195A (en) * 2021-06-02 2021-10-08 罗永文 Device for preventing polymerized ferrous sulfate floccule from blocking pump opening
CN113897754A (en) * 2021-11-16 2022-01-07 浙江吉和卫生材料有限公司 Melt-blown fabric manufacturing equipment with waste gas purification function
CN114669260A (en) * 2022-04-13 2022-06-28 江西轻竺科技股份有限公司 Split charging device for resin production and implementation method thereof
CN115155495A (en) * 2022-07-14 2022-10-11 洛阳中硅高科技有限公司 Preparation system and preparation method

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20010004666A1 (en) * 1999-09-14 2001-06-21 Kaneka Corporation Method of stripping for latex of vinyl chloride paste resin, stripping apparatus, and vinyl chloride paste resin latex having low concentration of residual monomer
CN201357070Y (en) * 2009-02-04 2009-12-09 宁波科博特钴镍有限公司 Spherical cobaltosic oxide reaction kettle
KR20130071186A (en) * 2011-12-20 2013-06-28 주식회사 포스코 Apparatus and method for refining silicon
CN205109642U (en) * 2015-11-18 2016-03-30 林素珠 Balanced type reactor stirrer with dust collector
CN105728122A (en) * 2016-03-10 2016-07-06 安徽省全椒未来饲料有限责任公司 Feedstuff crushing and proportioning machine
CN205613415U (en) * 2016-05-03 2016-10-05 黄翀 Prevent static reation kettle with tail gas processing apparatus
CN105999899A (en) * 2016-06-27 2016-10-12 浙江飞越洁具制造有限公司 Waste gas treatment apparatus for glass paint-spraying
CN206262548U (en) * 2016-12-05 2017-06-20 安佐化学有限公司 It is a kind of to be weighed integral type reaction kettle device for waste gas purification

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20010004666A1 (en) * 1999-09-14 2001-06-21 Kaneka Corporation Method of stripping for latex of vinyl chloride paste resin, stripping apparatus, and vinyl chloride paste resin latex having low concentration of residual monomer
CN201357070Y (en) * 2009-02-04 2009-12-09 宁波科博特钴镍有限公司 Spherical cobaltosic oxide reaction kettle
KR20130071186A (en) * 2011-12-20 2013-06-28 주식회사 포스코 Apparatus and method for refining silicon
CN205109642U (en) * 2015-11-18 2016-03-30 林素珠 Balanced type reactor stirrer with dust collector
CN105728122A (en) * 2016-03-10 2016-07-06 安徽省全椒未来饲料有限责任公司 Feedstuff crushing and proportioning machine
CN205613415U (en) * 2016-05-03 2016-10-05 黄翀 Prevent static reation kettle with tail gas processing apparatus
CN105999899A (en) * 2016-06-27 2016-10-12 浙江飞越洁具制造有限公司 Waste gas treatment apparatus for glass paint-spraying
CN206262548U (en) * 2016-12-05 2017-06-20 安佐化学有限公司 It is a kind of to be weighed integral type reaction kettle device for waste gas purification

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
陈乙崇: "《搅拌设备设计》", 30 November 1985 *

Cited By (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107983287A (en) * 2017-12-16 2018-05-04 河南莱帕克化工设备制造有限公司 resin polymerization pilot experiment system
CN108404815A (en) * 2018-04-12 2018-08-17 潘玉娇 A kind of polyurethane water-proof paint manufacturing and processing equipment
CN108514853A (en) * 2018-07-03 2018-09-11 台州道致科技股份有限公司 A kind of solid automatic feeding system
CN108816166A (en) * 2018-07-11 2018-11-16 协建(江苏)智能装备有限公司 A kind of chemical reaction reaction kettle of automatic Regulation
CN110109412A (en) * 2019-06-04 2019-08-09 珂黎艾(上海)环保科技有限公司 A kind of dosing control unit of vehicle tail gas emission control clarifier production
CN110975734A (en) * 2019-12-17 2020-04-10 湖州联科粘合剂有限公司 Stirring process for producing formaldehyde-free white glue
CN111604021B (en) * 2020-06-05 2022-04-08 舟山欧莱克新材料科技有限公司 Oxidation reaction system for preparing red-based KD and control method thereof
CN111604021A (en) * 2020-06-05 2020-09-01 舟山欧莱克新材料科技有限公司 Oxidation reaction system for preparing red-based KD and control method thereof
CN112791680A (en) * 2020-12-24 2021-05-14 华阳新材料科技集团有限公司 A nickel phosphorus complex synthesis system for adiponitrile production
CN113041982A (en) * 2021-03-18 2021-06-29 河南鑫利安全技术服务有限责任公司 Hazardous chemicals processing equipment with warning device
CN113137607A (en) * 2021-04-25 2021-07-20 浙江宏电环保装备有限公司 Waste gas particle treatment device and use method thereof
CN113244810A (en) * 2021-05-11 2021-08-13 陈燕利 Efficient reaction kettle for water-based ink production and production process thereof
CN113477195A (en) * 2021-06-02 2021-10-08 罗永文 Device for preventing polymerized ferrous sulfate floccule from blocking pump opening
CN113897754A (en) * 2021-11-16 2022-01-07 浙江吉和卫生材料有限公司 Melt-blown fabric manufacturing equipment with waste gas purification function
CN113897754B (en) * 2021-11-16 2023-09-05 浙江吉和卫生材料有限公司 Melt-blown cloth manufacture equipment with exhaust purification function
CN114669260A (en) * 2022-04-13 2022-06-28 江西轻竺科技股份有限公司 Split charging device for resin production and implementation method thereof
CN115155495A (en) * 2022-07-14 2022-10-11 洛阳中硅高科技有限公司 Preparation system and preparation method
CN115155495B (en) * 2022-07-14 2024-03-19 洛阳中硅高科技有限公司 Preparation system and preparation method

Similar Documents

Publication Publication Date Title
CN106622073A (en) Waste gas purifying and weighing integrated reaction kettle device
CN106732252A (en) A kind of waste gas purification apparatus of multifunctional reaction still
CN206262548U (en) It is a kind of to be weighed integral type reaction kettle device for waste gas purification
CN106622074A (en) Weighing-supportive reaction kettle device for preparing acrylate adhesive
CN107754750A (en) A kind of Chemical Manufacture combined reaction kettle
CN206262549U (en) A kind of weighed reaction kettle device for preparing acrylate adhesive
CN205889607U (en) A kneading machine for producing new material masterbatch
CN208087503U (en) Feces of livestock and poultry organic fertilizer complexes
CN207533222U (en) A kind of self-priming lotion screen printing brush coating reaction kettle of stirring
CN111893041A (en) Collagen enzymolysis reaction device
CN106732253A (en) One kind filters integrated reactor of weighing
CN208526424U (en) A kind of feed mixing machine with dedusting function
CN206229357U (en) A kind of waste gas purification apparatus of multifunctional reaction still
CN107772520A (en) A kind of premixed feed dispensing mixing apparatus and feed production system
CN109610426B (en) Movable algae collecting-composting integrated device
CN211098215U (en) Dustproof powder agitating unit
CN211070020U (en) Powder mixing and stirring system
CN216005696U (en) Aerobic composting device for solid agricultural wastes under laboratory conditions
CN212651754U (en) Be used for prosthetic microorganism mixing arrangement of soil
CN207941479U (en) A kind of coating material production mixing arrangement
CN210905971U (en) Lime production filters agitating unit
CN208642641U (en) A kind of cycle of ozone aeration stirring reaction kettle
CN112705090A (en) Preparation facilities of modified epoxy
CN211613774U (en) Explosion-proof metal powder processing device
CN209205093U (en) A kind of adhesive producing efficient mixing device

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
RJ01 Rejection of invention patent application after publication

Application publication date: 20170510

RJ01 Rejection of invention patent application after publication