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CN109290296A - A kind of clean method of reaction kettle colloid reaction residue - Google Patents

A kind of clean method of reaction kettle colloid reaction residue Download PDF

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Publication number
CN109290296A
CN109290296A CN201811094491.5A CN201811094491A CN109290296A CN 109290296 A CN109290296 A CN 109290296A CN 201811094491 A CN201811094491 A CN 201811094491A CN 109290296 A CN109290296 A CN 109290296A
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China
Prior art keywords
colloid
reaction kettle
residue
reaction
water
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Granted
Application number
CN201811094491.5A
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Chinese (zh)
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CN109290296B (en
Inventor
李艳芬
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Ningxia Fumei Environmental Protection Materials Co.,Ltd.
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Mianyang Flying Technology Co Ltd
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Priority to CN201811094491.5A priority Critical patent/CN109290296B/en
Publication of CN109290296A publication Critical patent/CN109290296A/en
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Publication of CN109290296B publication Critical patent/CN109290296B/en
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B08CLEANING
    • B08BCLEANING IN GENERAL; PREVENTION OF FOULING IN GENERAL
    • B08B7/00Cleaning by methods not provided for in a single other subclass or a single group in this subclass
    • B08B7/04Cleaning by methods not provided for in a single other subclass or a single group in this subclass by a combination of operations
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B08CLEANING
    • B08BCLEANING IN GENERAL; PREVENTION OF FOULING IN GENERAL
    • B08B7/00Cleaning by methods not provided for in a single other subclass or a single group in this subclass
    • B08B7/02Cleaning by methods not provided for in a single other subclass or a single group in this subclass by distortion, beating, or vibration of the surface to be cleaned

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  • Mixers Of The Rotary Stirring Type (AREA)

Abstract

The invention discloses a kind of method for cleaning of reaction kettle colloid reaction residue, and the method for cleaning cleaning colloid residue for solving existing reaction kettle is not thorough, and can be led to the problem of a large amount of waste water and be caused stress to environmental protection.The present invention include heat drying colloid, mechanical oscillation from reaction kettle body inner wall removing colloid residue, with a small amount of clear water colloid residue is taken away into reaction kettle body, colloid residue is separated from water.The present invention has many advantages, such as that reaction kettle body inner wall cleaning is thorough, environmentally friendly.

Description

A kind of clean method of reaction kettle colloid reaction residue
Technical field
The present invention relates to material Removal Technology fields, and in particular to a kind of cleaning side of reaction kettle colloid reaction residue Method.
Background technique
Reaction kettle is a kind of common reaction unit, is widely used in the fields such as chemical industry, medicine, material, especially prepares When colloidal substance, specifically, when producing colloid, reaction kettle after use, can remain colloid reaction object, due to anti-on inner wall Answering kettle is column vertical structure, bad cleaning, and existing technology is mostly to adopt to be rinsed with water or soaking and washing or Gas Stirring Cleaning etc., such method for cleaning can make colloid be homogenously mixed together with water, can not separate, in post-processing, also It needs waste liquid tune pH value and carries out sedimentation separation, and have that colloid is molten can not to be thoroughly kept completely separate in water always, in this way A large amount of waste water will be generated to cause stress for subsequent processing, and such manner of cleaning up colloid stronger for adhesiveness Material, depending cleaning alone can not completely remove, and use there are also inventor and install cleaning ring in reaction kettle body, but cleaning ring Always there is dead end of cleanning, can not clear up thoroughly, the later period is cleaned there is still a need for clear water.
Summary of the invention
The technical problems to be solved by the present invention are: the method for cleaning cleaning colloid residue of existing reaction kettle is not thorough Bottom, and a large amount of waste water can be generated, environmental protection is caused stress.
The present invention provides a kind of clean methods of the reaction kettle colloid reaction residue to solve the above problems.
The present invention is achieved through the following technical solutions:
A kind of clean method of reaction kettle colloid reaction residue, includes the following steps:
Step 1: it opens heating element and is heated;
Step 2: moving up and down inner shaft, adjusts the angle of agitating paddle, and the inner wall of the end and reaction kettle body that make agitating paddle connects Touching;
Step 3: opening the motor of mechanical oscillation stick, drives mechanical vibrating head vibration, and dry colloid is peeled off from inner wall It falls into reaction kettle body bottom and forms colloid residue;
Step 4: being added a small amount of water and colloid mixes outside merga pass discharge port discharge reaction kettle body;
Step 5: colloid residue and water are separated by solid-liquid separation.
The present invention utilizes colloid drying and dehydrating, and hardened lump is agglomerated between molecule, and viscosity sharply declines to nothing Method is adhered on the inner wall of reaction kettle body, realizes that Automatic-falling passes through mechanical oscillation for the drying colloid that can not be completely fallen off The effect of vibration of stick drives its peeling, then leads to too small amount of water for colloid residue band and separates out reaction kettle body, is finally consolidated again Liquid separation, this method Water usage is few, and hardened colloid residue will not be redissolved in water, and water is intended only as colloid residue row Medium outside reaction kettle body out, can be with direct emission after separation, environmental protection, and cleaning is thorough.
In order to guarantee that colloid can be by abundant dried cake, preferably a kind of cleaning of reaction kettle colloid reaction residue of the present invention Method, in the step 1, the temperature of heating is 80-150 DEG C, and the time of heating is 4-12 hour, by the operation so that suddenly The water content of nurse stone colloid is reduced to 10% by 70% or so, and according to drying principles, the water of colloid surface is first evaporated and dried, residual The a small amount of water stayed can be locked in the inside of colloid, at this point, the volume of Boehmite Sol can substantially be shunk, agglomerate and alice occur, It can fall off from reaction kettle inner wall to most of, leave behind small part and be slightly attached on inner wall.
Preferably, the water content after the colloid is dry is 0-5%, agglomerates and is broken in colloid residue in this way When, internal unseasoned complete colloid amount significantly reduces, and is not easy to be dispersed in water phase.
Preferably a kind of clean method of reaction kettle colloid reaction residue of the present invention is added a small amount of in the step 4 Water be to take the Boehmite Sol residue to fall off from reaction kettle body inner wall out of reaction kettle body by the effect of water flow Outside, the mixing includes: to adjust the angle of agitating paddle, makes it diagonally downward, opens speed regulating motor driving agitating shaft rotation, thus Agitating paddle rotation is driven to be stirred mixing to colloid residue and water, it is close apart from bottom since agitating paddle tilts down, it can be formed Very strong stirring power has agitaion to the colloid residue of reaction kettle body bottom, plays and help to the mixing of colloid residue and water Effect is pushed away, since the colloid residue on reaction kettle inner wall falls to reaction kettle body bottom by dry and mechanical oscillation, is not necessarily to Reaction kettle body inner wall is cleared up again, and only needs to take out of the colloid residue for falling to reaction kettle body bottom, at this point, only Need a small amount of water flowing that colloid residue is driven not precipitate, it is different from traditional colloid of being cleared up under water environment, in order to Inner wall residue is carried out to wash away removal, needs to fill almost entire reaction kettle body inner wall, and wash away and fall to by stirring Colloid in water will disperse in water, since the partial size very little of colloid is nanoscale, can generate so largely with dispersion agent The waste water of body, wastewater treatment capacity is big, and needs to adjust pH value and come so that the layering of colloid residue wastewater sedimentation, processing cost Height, it is also different for the existing mode struck off from the top down only by scraper plate, when striking off, struck off due to existing always Less than dead angle, such as the intersection of the side wall of reaction kettle body and bottom, and scrapings deposit to the colloid of bottom can not It is rejected to outside reaction kettle body, it is still desirable to which water carries out mixing and takes out of, but equally exists colloid in normal state and will disperse in water It is middle to form diluted colloidal solution waste water, need to adjust pH value to be layered, processing is cumbersome, at high cost and the high pH value of generation useless Water not environmentally present invention take advantage of that forming lump after colloid is dry, and is no longer disperse in water, without adjusting pH value, the PH of water Value still keeps neutral, can preferably realize separation of solid and liquid without a large amount of water.
The step of preferably a kind of clean method of reaction kettle colloid reaction residue of the present invention, the separation of solid and liquid are as follows: will The mixture of colloid residue and water by the filter screen of 400-800 mesh so that water pass through filter screen obtain upper layer colloid residue and Lower layer's waste liquid.
The step of preferably a kind of clean method of reaction kettle colloid reaction residue of the present invention, the separation of solid and liquid are as follows: will The mixture of colloid residue and water stands 4-24 hours, and upper layer waste liquid is then obtained by way of toppling over and lower layer's colloid is residual Slag.
The above water come out that is separated by solid-liquid separation takes the medium of colloid residue out of due to being intended only as, and is carrying out being separated by solid-liquid separation it Afterwards, because colloid is not dispersed in water, the pH value of water does not change, also reusable in the processing of next colloid residue, real It now reuses, reduces the use of water.
Preferably a kind of clean method of reaction kettle colloid reaction residue of the present invention, the liner material of the reaction kettle body are The intensity of polytetrafluoroethylene (PTFE), polytetrafluoroethylene (PTFE) is high, and resistance to acid and alkali is strong, and has hydrophobicity, more holds after Boehmite Sol is dry Easily fall off from reaction kettle inner wall.
Preferably a kind of clean method of reaction kettle colloid reaction residue of the present invention, reaction kettle used in this method, including Support construction, reaction kettle body, agitating device and mixer drive, are arranged collet on the outside of the reaction kettle body, in the collet Be arranged heating element, the reaction kettle body top setting with the matched lid of the reaction kettle body, the reaction kettle body it is interior Discharge port is arranged in side bottom end mounting temperature sensor, the bottom of the reaction kettle body, and feed opening is arranged on the lid, described anti- It answers and agitating device is set inside autoclave body,
The support construction includes pedestal, level support platform and column, and one end that uprights vertical is set on the base is described Level support platform is mounted on the top of column and parallel with pedestal, and the reaction kettle body is placed on pedestal,
The agitating device includes agitating paddle and hollow agitating shaft, and the lower end of the agitating shaft connects multiple agitating paddles, The agitating paddle protrudes into the distribution of the axially spaced-apart in the reaction kettle body and along agitating shaft, and the agitating paddle includes along the stirring First paddle of axial symmetry setting and the second paddle and connect with the agitating shaft by angle demodulator, the agitating paddle is with internal Mechanical oscillation stick is arranged in cavity, the internal cavities, and the horizontal length of the agitating paddle is equal to the inner chamber body of the reaction kettle body Width.
By the agitating paddle in reaction kettle body be set as can the structure of up and down adjustment angle pass through angle when preparing colloid Adjuster adjusts agitating paddle and tilts upwards, and required material is added in reaction kettle body by feed opening, closes feed opening and carries out Compressive reaction is heated, after generating colloid, cooling release, then pass through discharge hole for discharge.When needing to clear up the intracorporal residual of reaction kettle When colloid, discharge port is closed, opening heating element makes its heating, and a large amount of water is contained inside colloid, in a heated condition can be from It gradually dehydrates outside to inside, volume is largely shunk, and be hardened agglomeration, to remove with reaction kettle body inner wall, part is directly removed Fall into reaction kettle body bottom, part still can be attached on the inner wall of reaction kettle body, adjust angle demodulator so that agitating paddle to Lower rotation, when agitating paddle rotates down, can contradict because the length of agitating paddle is equal to the width of reaction kettle body inner chamber body To reaction kettle body inner wall, and during adjusting the first paddle and the second paddle and being drawn close to reaction kettle inner wall, the end of agitating paddle with For inner wall from when just touching last end face full contact reaction kettle inner wall, the end of agitating paddle can be to the glue on reaction kettle inner wall Body residue plays the role of striking off, and one eliminates colloid residue herein, it can also be ensured that the end of agitating paddle and anti- The full contact for answering inner wall of kettle enables mechanical energy more to pass to reaction kettle body inner wall, reduces the colloid because of alice The presence of residue and be lost caused by mechanical energy, after full contact open mechanical oscillation stick, mechanical oscillation are to reaction kettle The colloid residue vibration of inner wall makes it fall off, this outside anti-autoclave body relative to being arranged mechanical vibration equipment, on mechanical oscillation stick Mechanical wave stirred tank inner wall can be directly passed to by agitating paddle because the thickness of agitating paddle is smaller, the loss of mechanical wave It is small and more mechanical waves, which are transmitted on the inner wall of reaction kettle body, makes colloid residue fall off, in addition the first paddle and the second paddle Be it is symmetrically arranged, the energy vibrated on the inner wall contacted with reaction kettle is identical and symmetrical, this is relative to outside reaction kettle body Portion somewhere is arranged for mechanical oscillation, can reduce because of influence of the mechanical oscillation to the stability of reaction kettle body, machinery is shaken Dynamic stick be arranged in inside agitating paddle can also open agitating shaft motor control agitating shaft rotation vibrated in different directions, The application carries out the dry of residual colloid by the characteristic of colloid and clears up, and avoids traditional cleaning that is soaked in water and is not thorough, and A large amount of waste water are generated to cause stress to environmental protection or need to adjust pH value and could handle asking for the colloidal solution being distributed in water phase Topic.
Scraper plate is arranged in the end of a kind of currently preferred reaction kettle, the agitating paddle, and the scraper plate is that side is isosceles The prismatoid that the end of trapezoidal slave agitating paddle is gradually increased outward is needing to vibrate the glue on cleaning reaction inner wall of kettle in this way Body residue and adjust in the motion process of agitating paddle upward or downward, trapezoidal bottom edge corner angle can be to residual on reaction kettle body inner wall The colloid stayed is preferably struck off, and the length on bottom edge is longer, can more strike off the colloid on reaction kettle body inner wall, Floor space is also bigger, and the area contacted with reaction kettle body inner wall is also bigger, more preferable to the mechanical oscillation effect of reaction kettle body inner wall.
A kind of currently preferred reaction kettle, the agitating shaft are hollow structure, setting interspersed two in the hollow structure Side is provided with the inner shaft of the gear teeth, is equipped with the gear with the gear teeth meshing inside the angle demodulator, and the one of the agitating paddle End is fixedly connected with gear.
The mixer drive includes that motor, belt, the agitating shaft sequentially pass through the lid and institute from bottom to top Level support platform is stated, the agitating shaft in level support platform is provided with runner, and the runner passes through belt and motor Runner connection, motor runner lower end is fixed with motor.
In order to reduce the adhesion strength of dry colloid and reaction kettle body, the liner material selection polytetrafluoroethyl-ne of the reaction kettle body Alkene, polytetrafluoroethylene (PTFE) are a kind of smooth, acid-fast alkali-proof highstrenghtpiston resistant to high temperature, have hydrophobicity, after colloid is dry, easily In falling off from polytetrafluoroethylliner liner.
In order to further enhance mechanical oscillation suffered by reaction kettle liner, the quantity of the agitating paddle is 3, and each stirring Mechanical oscillation stick is respectively provided in the first paddle and the second paddle of paddle.
The present invention has the advantage that and the utility model has the advantages that
1. the present invention by heating, vibration, mixing, discharging, separate the step of to reaction kettle prepare after colloid to colloid into Row cleaning, method environmental protection, cleaning are thorough.
2. it is reaction kettle body liner material that the present invention, which selects polytetrafluoroethylene (PTFE), so that colloid is easier to slide and shell after dry From.
Detailed description of the invention
Attached drawing described herein is used to provide to further understand the embodiment of the present invention, constitutes one of the application Point, do not constitute the restriction to the embodiment of the present invention.In the accompanying drawings:
Fig. 1 is flow diagram of the invention.
Fig. 2 is reaction kettle of the invention in stirring flowering structure schematic diagram.
Fig. 3 is the structural schematic diagram under vibration condition of the present invention.
Label and corresponding parts title in attached drawing:
1- reaction kettle body, 2- discharge port, 3- pedestal, 4- level support platform, 5- column, 7- agitating paddle, 72- scraper plate, 8- are stirred Mix axis, 9- mechanical oscillation stick, 10- speed regulating motor, 11- heating element, 12- angle demodulator, 13- feed opening, 14- lid, 15- collet, 16- inner shaft, 17- belt, 18- runner, 19- motor runner, 20- temperature sensor, 21- limit card slot, 22- limit Column.
Specific embodiment
To make the objectives, technical solutions, and advantages of the present invention clearer, below with reference to embodiment and attached drawing, to this Invention is described in further detail, and exemplary embodiment of the invention and its explanation for explaining only the invention, are not made For limitation of the invention.
Embodiment 1
As shown in Figure 1, a kind of clean method of reaction kettle colloid reaction residue, includes the following steps:
Step 1: opening heating element 11 and heated, and heating temperature is 150 DEG C, and heating time is 4 hours;
Step 2: moving up and down inner shaft 16, adjusts the angle of agitating paddle 7, makes the end of agitating paddle 7 and reaction kettle body 1 Inner wall contact;
Step 3: opening the motor of mechanical oscillation stick 9, drives mechanical vibrating head 9 to vibrate, dry colloid is shelled from inner wall It falls and falls into 1 bottom of reaction kettle body formation colloid residue;
Step 4: adjusting the angle of agitating paddle 7, make it diagonally downward, opens speed regulating motor 10 and agitating shaft 8 is driven to rotate, To drive the rotation of agitating paddle 7 to be stirred mixing to colloid residue and water, and it is discharged outside reaction kettle body 1 by discharge port 2;
Step 5: colloid residue and water are separated by solid-liquid separation, and specifically, the mixture of colloid residue and water is passed through The filter screen of 800 mesh, so that water passes through filter screen and obtains upper layer colloid residue and lower layer's waste liquid.
Upper layer colloid residue is handled as solid refuse, and lower layer's waste liquid can direct emission.
Embodiment 2
The present embodiment the difference from embodiment 1 is that, the heating temperature of the step 1 is 80 DEG C, the time of the heating It is 12 hours, the solid-liquid separating method of the step 5 are as follows: the mixture of colloid residue and water is stood 12 hours, is then led to It crosses the mode toppled over and obtains upper layer waste liquid and lower layer's colloid residue, lower layer's colloid residue is handled as solid refuse, and on Layer waste clear solution can direct emission.
Embodiment 3
Reaction kettle used in a kind of clean method of reaction kettle colloid reaction residue as shown in Figures 2 and 3, including branch Collet 15, the collet are arranged on the outside of the reaction kettle body 1 for support structure, reaction kettle body 1, agitating device and mixer drive Heating element 11 is set in 15, and top setting and the matched lid 14 of the reaction kettle body 1 of the reaction kettle body 1 are described anti- The inner lower edge mounting temperature sensor 20 of autoclave body 1 is answered, discharge port 2, the lid 14 is arranged in the bottom of the reaction kettle body 1 Agitating device is arranged inside the reaction kettle body 1 in upper setting feed opening 13,
The support construction includes pedestal 3, level support platform 4 and column 5, and column 5 is vertically arranged one on the base 3 End, the level support platform 4 are mounted on the top of column 5 and parallel with pedestal 3, the placement of reaction kettle body 1 on the base 3,
The agitating device includes agitating paddle 7 and hollow agitating shaft 8, and the lower end of the agitating shaft 8 connects multiple stirrings Paddle 7, the agitating paddle 7 are protruded into the reaction kettle body 1 and are distributed along the axially spaced-apart of agitating shaft 8, and the agitating paddle 7 includes edge It symmetrically arranged first paddle of the agitating shaft 8 and the second paddle and is connect with the agitating shaft 8 by angle demodulator 12, it is described to stir Paddle 7 is mixed with internal cavities, mechanical oscillation stick 9 is arranged in the internal cavities, and the horizontal length of the agitating paddle 7 is equal to described anti- Answer the width of the inner chamber body of autoclave body 1.
Scraper plate 72 is arranged in the end of the agitating paddle 7, and the scraper plate 72 is the slave agitating paddle 7 that side is isosceles trapezoid The prismatoid that end is gradually increased outward.
The quantity of the agitating paddle 7 is 3, and the lower section along the agitating shaft 8 is uniformly distributed.
The liner material of the reaction kettle body 1 is 316L stainless steel.
The route of the mechanical oscillation stick 9 is connect by the cavity of agitating shaft 8 with external vibration motor.
The bottom of the reaction kettle body 1 is provided with stabilizer blade, and is placed on pedestal 3.
Specific working mode is: when preparing colloid, adjusting agitating paddle 7 by angle demodulator 12 and upwardly or downwardly inclines Tiltedly, required material is added in reaction kettle body 1 by feed opening 13, closes feed opening 13 and carry out heating compressive reaction, generates After colloid, cooling release, then discharged by discharge port 2.When needing to clear up the residual colloid in reaction kettle body 1, heating is opened Element 11 makes its heating, contains a large amount of water inside colloid, can gradually dehydrate in a heated condition, and volume is largely shunk, Be hardened agglomeration, to remove with 1 inner wall of reaction kettle body, part directly removing falls into 1 bottom of reaction kettle body, and part still can be adhered to On the inner wall of reaction kettle body 1, angle demodulator 12 is adjusted, so that agitating paddle 7 rotates down, because the length of agitating paddle 7 is Equal to the width of 1 inner chamber body of reaction kettle body, when agitating paddle 7 rotates down, 1 inner wall of reaction kettle body can be contradicted, at this point, The motor of mechanical oscillation stick 9 is opened, mechanical oscillation can occur for mechanical oscillation stick 9, and pass through agitating paddle 7 for the mechanical energy of vibration The inner wall of reaction kettle body 1 is passed to which the colloid for drying stripping and slicing get off from the interior wall vibrations of reaction kettle body 1, can also be opened The rotation of motor control agitating shaft 8 of agitating shaft 8 is vibrated in different directions.
Embodiment 4
The present embodiment and the difference of embodiment 3 are that the agitating shaft 8 is hollow structure, are arranged in the hollow structure Interspersed two sides are provided with the inner shaft 16 of the gear teeth, and the gear with the gear teeth meshing is equipped with inside the angle demodulator 12, described One end of agitating paddle 7 is fixedly connected with gear, the mixer drive include motor, belt 17, the agitating shaft 8 from it is lower to On sequentially pass through the lid 14 and the level support platform 4, the agitating shaft 8 in level support platform 4 is provided with Runner 18, the runner 18 are connect by belt 17 with motor runner 19, and 19 lower end of motor runner and speed regulating motor 10 are solid Fixed, the 18 upside agitating shaft 8 of runner is equipped with limit hole, and 18 downside agitating shaft 8 of runner is equipped with limited post 22, limited post 22 Downside agitating shaft 8 be equipped with angle demodulator 12, angle demodulator 12 about agitating shaft 8 be symmetrical arranged there are two, angular adjustment The gear of cooperation inner shaft 16 is equipped with inside device 12, gear is fixed on agitating shaft 8 by shaft, agitating paddle 7 is fixed on gear, The reaction kettle upper end is equipped with the limit card slot 21 of cooperation limited post 22.
The liner material of the reaction kettle body 1 is polytetrafluoroethylene (PTFE).
In the present invention, term " on " used, "lower", " in ", "bottom", "top", "left", "right", " two sides ", "outside" " back side " Deng being subject to orientation shown in attached drawing.
Above-described specific embodiment has carried out further the purpose of the present invention, technical scheme and beneficial effects It is described in detail, it should be understood that being not intended to limit the present invention the foregoing is merely a specific embodiment of the invention Protection scope, all within the spirits and principles of the present invention, any modification, equivalent substitution, improvement and etc. done should all include Within protection scope of the present invention.

Claims (6)

1. a kind of method for cleaning of reaction kettle colloid reaction residue, which comprises the steps of:
Step 1: heating element (11) are opened and are heated;
Step 2: moving up and down inner shaft (16), adjusts the angle of agitating paddle (7), makes end and the reaction kettle body of agitating paddle (7) (1) inner wall contact;
Step 3: opening the motor of mechanical oscillation stick (9), drives mechanical vibrating head (9) to vibrate, dry colloid is shelled from inner wall It falls and falls into the reaction kettle body (1) bottom formation colloid residue;
Step 4: being added a small amount of water and colloid mixes merga pass discharge port (2) and the reaction kettle body (1) is discharged outside;
Step 5: colloid residue and water are separated by solid-liquid separation.
2. a kind of method for cleaning of reaction kettle colloid reaction residue according to claim 1, which is characterized in that the step In rapid one, the temperature of heating is 80-150 DEG C, and the time of heating is 4-12 hours.
3. a kind of method for cleaning of reaction kettle colloid reaction residue according to claim 1 or 2, which is characterized in that In the step 4, the mixing includes: to adjust the angle of agitating paddle (7), makes it diagonally downward, opens speed regulating motor (10) and drives Dynamic agitating shaft (8) rotation, so that agitating paddle (7) rotation be driven to be stirred mixing to colloid residue and water.
4. a kind of method for cleaning of reaction kettle colloid reaction residue according to claim 1 or 2, which is characterized in that institute The step of stating separation of solid and liquid are as follows: the mixture of colloid residue and water is passed through to the filter screen of 400-800 mesh, so that water passes through filtering Net obtains upper layer colloid residue and lower layer's waste liquid.
5. a kind of method for cleaning of reaction kettle colloid reaction residue according to claim 1 or 2, which is characterized in that institute The step of stating separation of solid and liquid are as follows: the mixture of colloid residue and water is stood 4-24 hours, is then obtained by way of toppling over Upper layer waste liquid and lower layer's colloid residue.
6. a kind of method for cleaning of reaction kettle colloid reaction residue according to claim 1 or 2, which is characterized in that institute The liner material for stating reaction kettle body (1) is polytetrafluoroethylene (PTFE).
CN201811094491.5A 2018-09-19 2018-09-19 Method for cleaning reaction residues of reaction kettle colloid Active CN109290296B (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114308912A (en) * 2022-03-15 2022-04-12 山西互感器电测设备有限公司 Prebaked anode surface cleaning device

Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4373944A (en) * 1981-08-10 1983-02-15 Owens-Illinois, Inc. Removal of glass particles from glass articles
CN1304338A (en) * 1999-06-09 2001-07-18 巴工业株式会社 Method of washing rotating tube of horizontal type tubular centrifugal separator
CN1767892A (en) * 2003-03-28 2006-05-03 三得利株式会社 Solid matter discharge mechanism and discharge method
CN202289697U (en) * 2011-10-28 2012-07-04 济南大学 Water separation equipment
CN103382243A (en) * 2013-07-03 2013-11-06 大亚木业(江西)有限公司 Method used for cleaning glue residues in melamine urea-formaldehyde glue reaction vessel
CN203699991U (en) * 2014-02-19 2014-07-09 天津开发区威克达科技发展有限公司 Flushing and sewage-discharging device for sediment in a sodium hypochlorite liquid storage tank
CN105209184A (en) * 2013-03-15 2015-12-30 多明尼奥工程公司 Ultrasonically cleaning vessels and pipes
CN105880011A (en) * 2016-06-08 2016-08-24 安徽开发矿业有限公司 Method for clearing away obstinate impurities in high-intensity magnetic separator medium box
CN107262002A (en) * 2017-07-26 2017-10-20 汪培杰 A kind of reactor for being used to have colloid product
CN107983729A (en) * 2017-12-11 2018-05-04 上海航天设备制造总厂有限公司 Aluminium alloy pressure vessel taps frock and pressure vessel fifth wheel method for cleaning automatically

Patent Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4373944A (en) * 1981-08-10 1983-02-15 Owens-Illinois, Inc. Removal of glass particles from glass articles
CN1304338A (en) * 1999-06-09 2001-07-18 巴工业株式会社 Method of washing rotating tube of horizontal type tubular centrifugal separator
CN1767892A (en) * 2003-03-28 2006-05-03 三得利株式会社 Solid matter discharge mechanism and discharge method
CN202289697U (en) * 2011-10-28 2012-07-04 济南大学 Water separation equipment
CN105209184A (en) * 2013-03-15 2015-12-30 多明尼奥工程公司 Ultrasonically cleaning vessels and pipes
CN103382243A (en) * 2013-07-03 2013-11-06 大亚木业(江西)有限公司 Method used for cleaning glue residues in melamine urea-formaldehyde glue reaction vessel
CN203699991U (en) * 2014-02-19 2014-07-09 天津开发区威克达科技发展有限公司 Flushing and sewage-discharging device for sediment in a sodium hypochlorite liquid storage tank
CN105880011A (en) * 2016-06-08 2016-08-24 安徽开发矿业有限公司 Method for clearing away obstinate impurities in high-intensity magnetic separator medium box
CN107262002A (en) * 2017-07-26 2017-10-20 汪培杰 A kind of reactor for being used to have colloid product
CN107983729A (en) * 2017-12-11 2018-05-04 上海航天设备制造总厂有限公司 Aluminium alloy pressure vessel taps frock and pressure vessel fifth wheel method for cleaning automatically

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114308912A (en) * 2022-03-15 2022-04-12 山西互感器电测设备有限公司 Prebaked anode surface cleaning device
CN114308912B (en) * 2022-03-15 2022-05-24 山西互感器电测设备有限公司 Prebaked anode surface cleaning device

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