CN112742072B - High-temperature-resistant defoaming agent, production line and process - Google Patents
High-temperature-resistant defoaming agent, production line and process Download PDFInfo
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- CN112742072B CN112742072B CN202011481802.0A CN202011481802A CN112742072B CN 112742072 B CN112742072 B CN 112742072B CN 202011481802 A CN202011481802 A CN 202011481802A CN 112742072 B CN112742072 B CN 112742072B
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D19/00—Degasification of liquids
- B01D19/02—Foam dispersion or prevention
- B01D19/04—Foam dispersion or prevention by addition of chemical substances
- B01D19/0404—Foam dispersion or prevention by addition of chemical substances characterised by the nature of the chemical substance
- B01D19/0409—Foam dispersion or prevention by addition of chemical substances characterised by the nature of the chemical substance compounds containing Si-atoms
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D19/00—Degasification of liquids
- B01D19/02—Foam dispersion or prevention
- B01D19/04—Foam dispersion or prevention by addition of chemical substances
- B01D19/0404—Foam dispersion or prevention by addition of chemical substances characterised by the nature of the chemical substance
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/80—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis
- B01F27/96—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis with openwork frames or cages
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F33/00—Other mixers; Mixing plants; Combinations of mixers
- B01F33/80—Mixing plants; Combinations of mixers
- B01F33/81—Combinations of similar mixers, e.g. with rotary stirring devices in two or more receptacles
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F33/00—Other mixers; Mixing plants; Combinations of mixers
- B01F33/80—Mixing plants; Combinations of mixers
- B01F33/81—Combinations of similar mixers, e.g. with rotary stirring devices in two or more receptacles
- B01F33/813—Combinations of similar mixers, e.g. with rotary stirring devices in two or more receptacles mixing simultaneously in two or more mixing receptacles
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/10—Maintenance of mixers
- B01F35/12—Maintenance of mixers using mechanical means
- B01F35/121—Maintenance of mixers using mechanical means using a brush for cleaning out rests of products
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/40—Mounting or supporting mixing devices or receptacles; Clamping or holding arrangements therefor
- B01F35/42—Clamping or holding arrangements for mounting receptacles on mixing devices
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/45—Closures or doors specially adapted for mixing receptacles; Operating mechanisms therefor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/71—Feed mechanisms
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/71—Feed mechanisms
- B01F35/712—Feed mechanisms for feeding fluids
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Health & Medical Sciences (AREA)
- Toxicology (AREA)
- Dispersion Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Mixers Of The Rotary Stirring Type (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
Abstract
The invention discloses a high-temperature-resistant defoaming agent, a production line and a process, and in particular relates to the technical field of defoaming agents, and the technical scheme is as follows: the composite material comprises main materials and auxiliary materials, wherein the main materials (by weight) comprise: emulsified silicone oil: 15g-20g, organic silicon: 20g-30g of modified silicon polyether: 20g-35g of higher alcohol fatty acid ester complex: 10g-15g, linolenic acid: 6g-12g, stannous octoate: 6g-8g, wherein the auxiliary materials (by weight) comprise a thickener: 10g-20g, preservative: 5g-10g, including belt cleaning device, big box, box one, revolving stage and hollow tube, box one inner wall fixed mounting servo motor one, servo motor one output peg graft in box one inner wall, the beneficial effect of the invention is: through carrying out stirring mixing simultaneously when separating multiunit material, mix the back again with multiunit mixed material stirring mixing, not only practiced thrift the time like this, still improved output and reduced the input of cost.
Description
Technical Field
The invention relates to the field of defoamers, in particular to a high-temperature-resistant defoamer, a production line and a process.
Background
The defoaming agent, also called as defoaming agent, is a food additive which reduces surface tension in the food processing process, inhibits foam generation or eliminates foam generated, and is approved by China to be used for 7 types of emulsified silicone oil, high-carbon alcohol fatty acid ester compound, polyoxyethylene polyoxypropylene pentaerythritol ether, polyoxyethylene polyoxypropylene alcohol amine ether, polyoxypropylene glycerol ether, polyoxypropylene polyoxyethylene glycerol ether, polydimethylsiloxane and the like, is also called as a defoaming agent, a plurality of harmful foams can be generated in the industrial production process, and the defoaming agent needs to be added, so that the defoaming agent is widely applied to removing the harmful foams generated in the industrial production processes of latex, textile sizing, food fermentation, biological medicine, pesticides, coatings, petrochemical industry, papermaking, industrial cleaning and the like, and is required to be sequentially stirred and mixed in the production process.
The prior art has the following defects: the existing stirring device generally needs to be cleaned after stirring and mixing a group of materials, and then the next group of materials are stirred, so that time is wasted, and the yield of the defoaming agent is reduced.
Therefore, it is necessary to invent a high temperature resistant defoamer, a production line and a process.
Disclosure of Invention
Therefore, the invention provides a high-temperature-resistant defoaming agent, a production line and a process, wherein a rotating rotary table is used for moving a corresponding small stirring box to a hollow pipe, then the hollow pipe flows corresponding materials into the small stirring box, and then the hollow pipe is cleaned by a cleaning device, so that the problem that the conventional stirring device generally needs to clean the stirring device and then stir the next group of materials after stirring and mixing the group of materials is solved.
In order to achieve the above object, the present invention provides the following technical solutions: the high-temperature-resistant defoaming agent comprises a main material and auxiliary materials, wherein the main material (by weight) comprises: emulsified silicone oil: 15g-20g, organic silicon: 20g-30g of modified silicon polyether: 20g-35g of higher alcohol fatty acid ester complex: 10g-15g, linolenic acid: 6g-12g, stannous octoate: 6g-8g, wherein the auxiliary materials (by weight) comprise a thickener: 10g-20g, preservative: 5g-10g.
The high-temperature-resistant defoaming agent production line comprises a cleaning device, a large box body, a first box body, a rotary table and a hollow pipe, wherein a first servo motor is fixedly installed on the inner wall of the first box body, an output end of the first servo motor is inserted into the inner wall of the first box body, a first hydraulic cylinder is fixedly installed on the inner wall of the first box body, and an output end of the first hydraulic cylinder is inserted into the inner wall of the rotary table;
the inner wall of the top end of the rotary table is in square arrangement and is in threaded connection with a small stirring box, a first partition board is inserted into the inner wall of the bottom end of the small stirring box, a second box body is fixedly arranged on the inner wall of the bottom end of the small stirring box, a second servo motor is fixedly arranged on the inner wall of the second box body, and the output end of the second servo motor penetrates through the first partition board and is inserted into the inner wall of the first stirrer;
the inner wall of the middle end of the top of the rotary table is in threaded connection with a large stirring tank, a second partition board is inserted into the inner wall of the bottom end of the large stirring tank, a third tank body is fixedly arranged on the inner wall of the bottom end of the large stirring tank, a third servo motor is fixedly arranged on the inner wall of the third tank body, and the output end of the third servo motor penetrates through the second partition board and is inserted into the inner wall of the second stirrer;
a baffle is inserted into one end of the inner wall of the hollow pipe, a fourth box body is fixedly arranged at one end of the outer wall of the baffle, a fourth servo motor is fixedly arranged on the inner wall of the fourth box body, the output end of the fourth servo motor penetrates through the baffle and is inserted into the inner wall of a second box body, and a second hydraulic cylinder is fixedly arranged on the inner wall of the second box body;
the cleaning device comprises a first circular plate, the output end of the hydraulic cylinder II is inserted into the inner wall of the first circular plate, and brush wires are arranged on the circumference of the outer wall of the first circular plate.
Preferably, the cleaning device further comprises a second circular plate, the output end of the second hydraulic cylinder is inserted into the inner wall of the second circular plate, and the second circular plate is inserted into the inner wall of the sponge.
Preferably, the support columns are fixedly installed at two ends of the inner wall of the top of the large box body, the round cover plate is fixedly installed at the bottom of the support column, the U-shaped heating pipes are fixedly installed at the bottom of the round cover plate, and at least one group of U-shaped heating pipes is arranged.
Preferably, the first box body is fixedly arranged at the bottom of the large box body.
Preferably, the hollow tubes are inserted into the two ends of the inner wall of the large box body.
Preferably, the inner wall of the top end of the hollow tube is provided with a feed inlet.
Preferably, the small stirring tank and the large stirring tank are positioned below the U-shaped heating pipe.
Preferably, the output end of the hollow tube is positioned above the small stirring box.
The high temperature resistant defoaming agent process further comprises the following specific steps:
s1, starting a first servo motor, driving a hydraulic cylinder to rotate through a box body, driving a rotary table to rotate through the hydraulic cylinder, moving one group of small stirring boxes to a hollow pipe through the rotary table until the rotary table rotates, placing emulsified silicone oil and organic silicon in the hollow pipe through a feed inlet, enabling materials to flow into the small stirring boxes, and placing a modified silicon polyether and high-carbon alcohol fatty acid ester compound into the other group of small stirring boxes through the other group of hollow pipe after the materials flow into the small stirring boxes;
s2, when materials flow into the small stirring box, the first hydraulic cylinder drives the rotary table to ascend until the rotary table is higher than the hollow tube, then the fourth servo motor drives the second hydraulic cylinder to rotate through the second box body, the rotating hydraulic cylinder drives the brush wires to rotate and stretch through the first circular plate, so that the brush wires clear the inner wall of the hollow tube, and the rotary table is restored to the original position after clearing, so that the hollow tube can be kept clean all the time;
s3, moving the small stirring boxes without the materials to the hollow tubes through a first servo motor, putting linolenic acid and stannous octoate into one group of small stirring boxes through the hollow tubes after moving, and putting a thickening agent and a preservative into the other group of small stirring boxes through the other group of hollow tubes after moving;
s4, after materials are filled in the small stirring box, a rotary table is driven to rise through a hydraulic cylinder until the rotary table is attached to a round cover plate, after the attachment, a U-shaped heating pipe is started until the temperature in the small stirring box reaches the temperature required by the materials, wherein the temperature of emulsified silicone oil and organosilicon is 150 ℃, the temperature of a modified silicon polyether and high-carbon alcohol fatty acid ester compound is 120 ℃, the temperature of linolenic acid and stannous octoate is 130 ℃, and the temperature of a thickening agent and a preservative is 90 ℃;
s5, the first stirrer is driven to rotate by the second servo motor, the first stirrer is driven to stir and mix materials, after the materials are stirred and mixed, the rotary table is restored to the original position, the small stirring box is taken out of the rotary table, the mixed materials in the small stirring box are poured into the large stirring box after being taken out, the rotary table is lifted until the large stirring box is attached to the round cover plate, then the U-shaped heating pipe is started until the temperature in the large stirring box reaches 130 ℃, the third servo motor is driven to rotate, and the second stirrer is driven to stir and mix multiple groups of mixed materials.
The beneficial effects of the invention are as follows:
when the invention is used, the first servo motor drives the first hydraulic cylinder to rotate through the box body, then the first hydraulic cylinder drives the rotary table to rotate until the rotary table moves the corresponding small stirring box to the hollow pipe, then the corresponding material is placed in the hollow pipe through the feeding port, then the material flows into the small stirring box, when the material flows into the small stirring box, the first hydraulic cylinder drives the rotary table to rise until the rotary table is higher than the hollow pipe, then the fourth servo motor drives the second hydraulic cylinder to rotate through the second box, the second rotary hydraulic cylinder drives the brush wire to rotate and stretch through the circular plate, so that the brush wire cleans the inner wall of the hollow pipe, and then the rotary table is restored to the original position, so that the hollow pipe is kept clean at all times, and the defoaming agent quality is improved, when the material is placed in the corresponding small stirring box, the rotary table is attached to the circular cover plate, the U-shaped heating pipe is started until the temperature required by the material in the small stirring box is reached, then the first servo motor drives the first rotary table to rotate the circular plate, the brush wire is cleaned up to the inner wall of the hollow pipe, the rotary table is restored to the original position after the material is mixed, the material is mixed in the small stirring box is removed, the small stirring box is reached, the first stirring box is turned, the material is mixed, the first stirring box is completely is mixed, and then the material is mixed, after the first stirring box is completely is mixed, and the material is mixed, and the first stirring box is completely, the second rotary stirrer is used for stirring and mixing the multiple groups of mixed materials, and stirring and mixing are performed simultaneously when the multiple groups of materials are separated, so that the multiple groups of mixed materials are stirred and mixed after being mixed, the time is saved, the yield is improved, and the cost is reduced.
Drawings
FIG. 1 is a schematic front view of the structure of embodiment 1;
FIG. 2 is a schematic top view of the structure of embodiment 1 according to the present invention;
FIG. 3 is an enlarged schematic view of the front A area of the structure of example 1 according to the present invention;
FIG. 4 is an enlarged schematic view of region B in front view of the structure of example 1 according to the present invention;
FIG. 5 is an enlarged schematic view of region C in front view of the structure of example 1 according to the present invention;
FIG. 6 is an enlarged schematic view of the front D area of the structure of example 1 according to the present invention;
FIG. 7 is a schematic front view of the structure of embodiment 2 according to the present invention;
fig. 8 is an enlarged schematic diagram of the front E area of the structure of example 2 according to the present invention.
In the figure: the cleaning device 1, a circular plate I11, brush wires 12, a circular plate II 13, a sponge 14, a large box body 2, a supporting column 21, a circular cover plate 22, a U-shaped heating pipe 23, a box body I3, a servo motor I31, a box body I32, a hydraulic cylinder I33, a rotary table 4, a small stirring box 41, a box body II 411, a servo motor II 412, a partition plate I413, a stirrer I414, a large stirring box 42, a box body III 421, a servo motor III 422, a partition plate II 423, a stirrer II 424, a hollow pipe 5, a feed inlet 51, a box body IV 52, a servo motor IV 53, a baffle 54, a box body II 55 and a hydraulic cylinder II 56.
Detailed Description
The preferred embodiments of the present invention will be described below with reference to the accompanying drawings, it being understood that the preferred embodiments described herein are for illustration and explanation of the present invention only, and are not intended to limit the present invention.
The high-temperature-resistant defoaming agent comprises a main material and auxiliary materials, wherein the main material (by weight) comprises: emulsified silicone oil: 15g-20g, organic silicon: 20g-30g of modified silicon polyether: 20g-35g of higher alcohol fatty acid ester complex: 10g-15g, linolenic acid: 6g-12g, stannous octoate: 6g-8g, wherein the auxiliary materials (by weight) comprise a thickener: 10g-20g, preservative: 5g-10g.
Embodiment 1, refer to fig. 1-6, the invention provides a high temperature resistant defoamer production line, which comprises a cleaning device 1, a large box 2, a first box 3, a rotary table 4 and a hollow pipe 5;
further, the first servo motor 31 is fixedly installed on the inner wall of the first box body 3, the output end of the first servo motor 31 is inserted into the inner wall of the first box body 32, the first hydraulic cylinder 33 is fixedly installed on the inner wall of the first box body 32, the output end of the first hydraulic cylinder 33 is inserted into the inner wall of the rotary table 4, specifically, the first servo motor 31 is an engine for controlling mechanical elements to operate in a servo system and is an indirect speed changing device for assisting the motor, the first servo motor 31 is set AS JSF42-3-30-AS-1000, the first servo motor 31 has the function of driving the first hydraulic cylinder 33 to rotate through the first box body 32, the first hydraulic cylinder 33 is a hydraulic executing element for converting hydraulic energy into mechanical energy and performing linear reciprocating motion or swinging motion, the first hydraulic cylinder 33 is set AS CDM1, the first hydraulic cylinder 33 has the function of driving the rotary table 4 to rotate and lift, the rotary table 4 has the function of moving the corresponding small stirring box 41 to the hollow tube 5, and the lifting rotary table 4 has the function of closing the small stirring box 41 and the large stirring box 42 through the circular cover plate 22.
Further, the inner wall of the top end of the rotary table 4 is in square arrangement and is in threaded connection with the small stirring box 41, the inner wall of the bottom end of the small stirring box 41 is inserted with the first partition plate 413, the inner wall of the bottom end of the small stirring box 41 is fixedly provided with the second box 411, the inner wall of the second box 411 is fixedly provided with the second servo motor 412, the output end of the second servo motor 412 penetrates through the first partition plate 413 and is inserted into the inner wall of the first stirrer 414, specifically, the first partition plate 413 has the function of preventing materials from flowing into the bottom end of the small stirring box 41, the second servo motor 412 is arranged as SM 80-013-30LFB, the second servo motor 412 has the function of driving the first stirrer 414 to rotate, and the first stirrer 414 has the function of stirring and mixing the materials.
Further, the inner wall of the middle end of the top of the rotary table 4 is in threaded connection with the large stirring tank 42, the inner wall of the bottom end of the large stirring tank 42 is inserted with the second partition plate 423, the inner wall of the bottom end of the large stirring tank 42 is fixedly provided with the third box 421, the inner wall of the third box 421 is fixedly provided with the third servo motor 422, the output end of the third servo motor 422 penetrates through the second partition plate 423 and is inserted into the inner wall of the second stirrer 424, specifically, the second partition plate 423 has the function of preventing the mixed materials from flowing into the bottom end of the large stirring tank 42, the third servo motor 422 is set to be SM 110-060-30LFB, the third servo motor 422 has the function of driving the second stirrer 424 to rotate, and the second stirrer 424 has the function of stirring and mixing multiple groups of mixed materials.
Further, one end of the inner wall of the hollow tube 5 is inserted into a baffle 54, one end of the outer wall of the baffle 54 is fixedly provided with a fourth box 52, the inner wall of the fourth box 52 is fixedly provided with a fourth servo motor 53, the output end of the fourth servo motor 53 penetrates through the baffle 54 and is inserted into the inner wall of a second box 55, the inner wall of the second box 55 is fixedly provided with a second hydraulic cylinder 56, the hollow tube 5 has the function of circulating materials, the baffle 54 has the fixing function on the fourth box 52, the fourth servo motor 53 is set to SM 150-150-25LFB, the fourth servo motor 53 has the function of driving the second hydraulic cylinder 56 to rotate through the second box 55, and the second hydraulic cylinder 56 is set to 1508CW-NPT.
Further, the cleaning device 1 includes a first circular plate 11, an output end of the second hydraulic cylinder 56 is inserted into an inner wall of the first circular plate 11, a brush wire 12 is disposed on an outer wall circumference of the first circular plate 11, specifically, the second hydraulic cylinder 56 has a function of driving the first circular plate 11 to rotate and stretch, the first circular plate 11 has a function of driving the brush wire 12 to rotate and stretch, and the brush wire 12 has a function of cleaning an inner wall of the hollow tube 5.
Further, the supporting columns 21 are fixedly installed at two ends of the inner wall of the top of the large tank body 2, the round cover plate 22 is fixedly installed at the bottom of the supporting columns 21, the U-shaped heating pipes 23 are fixedly installed at the bottom of the round cover plate 22, at least one group of U-shaped heating pipes 23 are specifically arranged, the round cover plate 22 has the function of enabling the small stirring tank 41 and the large stirring tank 42 to be closed, so that materials are prevented from flowing out, the U-shaped heating pipes 23 have the function of improving the temperature in the small stirring tank 41 and the large stirring tank 42, and the U-shaped heating pipes 23 are preferably five groups.
Further, the first box 3 is fixedly installed at the bottom of the large box 2, and specifically, the large box 2 has a fixing effect on the first box 3.
Further, the hollow tubes 5 are inserted into two ends of the inner wall of the large box body 2, and specifically, the large box body 2 has a fixing effect on the hollow tubes 5.
Further, the inner wall of the top end of the hollow tube 5 is provided with a feed inlet 51, and specifically, the material is placed in the hollow tube 5 through the feed inlet 51.
Further, the small and large stirring tanks 41 and 42 are located below the U-shaped heating pipe 23, and specifically, the small and large stirring tanks 41 and 42 are located below the U-shaped heating pipe 23, which has the effect of facilitating the increase of the temperature in the small and large stirring tanks 41 and 42.
Further, the output end of the hollow tube 5 is located above the small stirring tank 41, and in particular, the output end of the hollow tube 5 is located above the small stirring tank 41 to have the effect of facilitating the material flowing into the small stirring tank 41.
The application process of the invention is as follows: when the invention is used, the first servo motor 31 drives the first hydraulic cylinder 33 to rotate through the first box body 32, then the first hydraulic cylinder 33 drives the rotary table 4 to rotate until the rotary table 4 moves one group of small stirring boxes 41 to the hollow tube 5, and then emulsified silicone oil is added: 15g-20g, preferably 17.5g and silicone: 20g-30g, preferably 25g, are placed in the hollow tube 5 through the feed inlet 51, and then the material flows into the small stirred tank 41, after which the modified silicone polyether is again: 20g-35g, preferably 27.5g and higher alcohol fatty acid ester complex: 10g-15g, preferably, 12.5g is put into another group of small stirring boxes 41 through another group of hollow tubes 5, when materials flow into the small stirring boxes 41, the first hydraulic cylinder 33 drives the rotary table 4 to ascend until the rotary table 4 is higher than the hollow tubes 5, then the fourth servo motor 53 drives the second hydraulic cylinder 56 through the second box body 55 to rotate, the second rotating hydraulic cylinder 56 drives the brush wires 12 to rotate and stretch through the first circular plate 11, so that the brush wires 12 clean the inner walls of the hollow tubes 5, the rotary table 4 is restored to the original position after cleaning, the hollow tubes 5 are kept clean all the time, then the small stirring boxes 41 which are not filled with materials are moved to the hollow tubes 5 through the first servo motor 31, and linolenic acid is added after the rotary table is moved to: 6g-12g, preferably 9g and stannous octoate: 6g-8g, preferably 7g, are placed through the hollow tube 5 into one of the small sets of stirred tanks 41, after which the thickener is added: 10g-20g, preferably 15g and preservative: 5g-10g, preferably 7.5g, are put into another group of small stirring boxes 41 through another group of hollow pipes 5, after materials are filled into the small stirring boxes 41, a first hydraulic cylinder 33 drives a rotary table 4 to rise until the rotary table 4 is attached to a round cover plate 22, after the materials are attached, a U-shaped heating pipe 23 is started until the temperature in the small stirring boxes 41 reaches the temperature required by the materials, wherein the temperature of the silicone emulsion and the temperature of the organosilicon are 150 ℃, the temperature of the modified silicon polyether and the high-carbon alcohol fatty acid ester compound are 120 ℃, the temperature of the linolenic acid and the stannous octoate are 130 ℃ and the temperature of the thickening agent and the preservative are 90 ℃, a second servo motor 412 drives a first stirrer 414 to rotate, the first rotating stirrer 414 stirs and mixes the materials, after stirring and mixing the materials, the rotary table 4 is restored to the original position, the small stirring box 41 is taken out from the rotary table 4, after taking out, the mixed materials in the small stirring box 41 are poured into the large stirring box 42, after pouring, the rotary table 4 is lifted until the large stirring box 42 is attached to the round cover plate 22, then the U-shaped heating pipe 23 is started until the temperature in the large stirring box 42 reaches 130 ℃, the third servo motor 422 drives the second stirrer 424 to rotate, the second rotating stirrer 424 stirs and mixes multiple groups of mixed materials, and the inner wall of the hollow pipe 5 is cleaned by the brush wires 12, so that the cleaning effect is improved.
Embodiment 2 referring to fig. 6-8, the high temperature resistant defoamer, the production line and the process provided by the invention comprise a cleaning device 1, a large box 2, a first box 3, a rotary table 4 and a hollow pipe 5;
further, the cleaning device 1 further comprises a second circular plate 13, the output end of the second hydraulic cylinder 56 is inserted into the inner wall of the second circular plate 13, the second circular plate 13 is inserted into the inner wall of the sponge 14, specifically, the second hydraulic cylinder 56 has the function of driving the second circular plate 13 to rotate and stretch, the second circular plate 13 has the function of driving the sponge 14 to rotate and stretch, and the sponge 14 has the function of cleaning the inner wall of the hollow tube 5.
The application process of the invention is as follows: when the invention is used, the first servo motor 31 drives the first hydraulic cylinder 33 to rotate through the first box body 32, then the first hydraulic cylinder 33 drives the rotary table 4 to rotate until the rotary table 4 moves one group of small stirring boxes 41 to the hollow tube 5, and then emulsified silicone oil is added: 15g-20g, preferably 17.5g and silicone: 20g-30g, preferably 25g, are placed in the hollow tube 5 through the feed inlet 51, and then the material flows into the small stirred tank 41, after which the modified silicone polyether is again: 20g-35g, preferably 27.5g and higher alcohol fatty acid ester complex: 10g-15g, preferably, 12.5g is put into another group of small stirring boxes 41 through another group of hollow tubes 5, when materials flow into the small stirring boxes 41, the first hydraulic cylinder 33 drives the rotary table 4 to ascend until the rotary table 4 is higher than the hollow tubes 5, then the fourth servo motor 53 drives the second hydraulic cylinder 56 through the second box body 55 to rotate, the second rotating hydraulic cylinder 56 drives the sponge 14 to rotate and stretch through the second circular plate 13, so that the sponge 14 cleans the inner wall of the hollow tubes 5, the rotary table 4 is restored to the original position after cleaning, the hollow tubes 5 are kept clean all the time, then the small stirring boxes 41 which are not filled with materials are moved to the hollow tubes 5 through the first servo motor 31, and linolenic acid is added after the movement: 6g-12g, preferably 9g and stannous octoate: 6g-8g, preferably 7g, are placed through the hollow tube 5 into one of the small sets of stirred tanks 41, after which the thickener is added: 10g-20g, preferably 15g and preservative: 5g-10g, preferably 7.5g, are put into another group of small stirring boxes 41 through another group of hollow pipes 5, after materials are filled into the small stirring boxes 41, a first hydraulic cylinder 33 drives a rotary table 4 to rise until the rotary table 4 is attached to a round cover plate 22, after the materials are attached, a U-shaped heating pipe 23 is started until the temperature in the small stirring boxes 41 reaches the temperature required by the materials, wherein the temperature of the silicone emulsion and the temperature of the organosilicon are 150 ℃, the temperature of the modified silicon polyether and the high-carbon alcohol fatty acid ester compound are 120 ℃, the temperature of the linolenic acid and the stannous octoate are 130 ℃ and the temperature of the thickening agent and the preservative are 90 ℃, a second servo motor 412 drives a first stirrer 414 to rotate, the first rotating stirrer 414 stirs and mixes the materials, after stirring and mixing the materials, the rotary table 4 is restored to the original position, the small stirring box 41 is taken out from the rotary table 4, after taking out, the mixed materials in the small stirring box 41 are poured into the large stirring box 42, after pouring, the rotary table 4 is lifted until the large stirring box 42 is attached to the round cover plate 22, then the U-shaped heating pipe 23 is started until the temperature in the large stirring box 42 reaches 130 ℃, the third servo motor 422 drives the second stirrer 424 to rotate, the second rotating stirrer 424 stirs and mixes multiple groups of mixed materials, and the sponge 14 is selected to clean the inner wall of the hollow pipe 5, so that scratches on the inner wall of the hollow pipe 5 are prevented.
Example 3:
the high temperature resistant defoaming agent process further comprises the following specific steps:
s1, starting a first servo motor 31, driving a first hydraulic cylinder 33 to rotate through a first box body 32 by the first servo motor 31, driving a rotary table 4 to rotate by the first hydraulic cylinder 33 until the rotary table 4 rotates to move one group of small stirring boxes 41 to the hollow pipe 5, placing emulsified silicone oil and organic silicon into the hollow pipe 5 through a feed inlet 51, allowing materials to flow into the small stirring boxes 41, and then placing a modified silicon polyether and high-carbon alcohol fatty acid ester compound into the other group of small stirring boxes 41 through the other group of hollow pipes 5;
s2, when materials flow into the small stirring box 41, the first hydraulic cylinder 33 drives the rotary table 4 to ascend until the rotary table 4 is higher than the hollow tube 5, then the fourth servo motor 53 drives the second hydraulic cylinder 56 to rotate through the second box body 55, the second rotating hydraulic cylinder 56 drives the brush wires 12 to rotate and stretch through the first circular plate 11, so that the brush wires 12 clean the inner wall of the hollow tube 5, and the rotary table 4 is restored to the original position after cleaning, so that the hollow tube 5 is kept clean all the time;
s3, moving the small stirring boxes 41 which are not filled with materials to the hollow tubes 5 through the first servo motor 31, putting linolenic acid and stannous octoate into one group of small stirring boxes 41 through the hollow tubes 5 after moving, and putting a thickening agent and a preservative into the other group of small stirring boxes 41 through the other group of hollow tubes 5 after moving;
s4, after materials are filled in the small stirring tank 41, the first hydraulic cylinder 33 drives the rotary table 4 to rise until the rotary table 4 is attached to the round cover plate 22, and after the attachment, the U-shaped heating pipe 23 is started until the temperature in the small stirring tank 41 reaches the temperature required by the materials, wherein the temperature of the emulsified silicone oil and the organosilicon is 150 ℃, the temperature of the modified silicon polyether and the high-carbon alcohol fatty acid ester compound is 120 ℃, the temperature of the linolenic acid and the stannous octoate is 130 ℃ and the temperature of the thickening agent and the preservative is 90 ℃;
s5, the second servo motor 412 drives the first stirrer 414 to rotate, the first rotating stirrer 414 stirs and mixes the materials, after the materials are stirred and mixed, the rotary table 4 is restored to the original position, the small stirring box 41 is taken out from the rotary table 4, the mixed materials in the small stirring box 41 are poured into the large stirring box 42 after being taken out, the rotary table 4 is lifted until the large stirring box 42 is attached to the circular cover plate 22, then the U-shaped heating pipe 23 is started until the temperature in the large stirring box 42 reaches 130 ℃, the third servo motor 422 drives the second stirrer 424 to rotate, and the second rotating stirrer 424 stirs and mixes multiple groups of mixed materials.
The above description is of the preferred embodiments of the present invention, and any person skilled in the art may modify the present invention or make modifications to the present invention with the technical solutions described above. Therefore, any simple modification or equivalent made according to the technical solution of the present invention falls within the scope of the protection claimed by the present invention.
Claims (8)
1. A high temperature resistant defoaming agent process is characterized in that: including high temperature resistant defoaming agent production line, high temperature resistant defoaming agent production line includes belt cleaning device (1), big box (2), box one (3), revolving stage (4) and hollow tube (5), its characterized in that: the inner wall of the first box body (3) is fixedly provided with a first servo motor (31), the output end of the first servo motor (31) is inserted into the inner wall of the first box body (32), the inner wall of the first box body (32) is fixedly provided with a first hydraulic cylinder (33), and the output end of the first hydraulic cylinder (33) is inserted into the inner wall of the rotary table (4);
the inner wall of the top end of the rotary table (4) is in square arrangement and is in threaded connection with a small stirring box (41), a first partition plate (413) is inserted into the inner wall of the bottom end of the small stirring box (41), a second box body (411) is fixedly arranged on the inner wall of the bottom end of the small stirring box (41), a second servo motor (412) is fixedly arranged on the inner wall of the second box body (411), and the output end of the second servo motor (412) penetrates through the first partition plate (413) and is inserted into the inner wall of the first stirrer (414);
the inner wall of the middle end of the top of the rotary table (4) is in threaded connection with a large stirring box (42), a second partition plate (423) is inserted into the inner wall of the bottom end of the large stirring box (42), a third box (421) is fixedly arranged on the inner wall of the bottom end of the large stirring box (42), a third servo motor (422) is fixedly arranged on the inner wall of the third box (421), and the output end of the third servo motor (422) penetrates through the second partition plate (423) and is inserted into the inner wall of a second stirrer (424);
a baffle plate (54) is inserted into one end of the inner wall of the hollow pipe (5), a fourth box body (52) is fixedly arranged at one end of the outer wall of the baffle plate (54), a fourth servo motor (53) is fixedly arranged on the inner wall of the fourth box body (52), the output end of the fourth servo motor (53) penetrates through the baffle plate (54) and is inserted into the inner wall of a second box body (55), and a second hydraulic cylinder (56) is fixedly arranged on the inner wall of the second box body (55);
the cleaning device (1) comprises a first circular plate (11), the output end of a second hydraulic cylinder (56) is inserted into the inner wall of the first circular plate (11), and brush wires (12) are arranged on the circumference of the outer wall of the first circular plate (11);
the method also comprises the following specific steps:
s1, starting a first servo motor (31), driving a first hydraulic cylinder (33) to rotate through a first box body (32), driving a rotary table (4) to rotate through the first hydraulic cylinder (33), moving one group of small stirring boxes (41) to a hollow pipe (5) through the rotary table (4), placing emulsified silicone oil and organic silicon into the hollow pipe (5) through a feed inlet (51), enabling materials to flow into the small stirring boxes (41), and then placing a modified silicon polyether and high alcohol fatty acid ester compound into the other group of small stirring boxes (41) through the other group of hollow pipes (5);
s2, when materials flow into the small stirring box (41), the first hydraulic cylinder (33) drives the rotary table (4) to ascend until the rotary table (4) is higher than the hollow tube (5), then the fourth servo motor (53) drives the second hydraulic cylinder (56) to rotate through the second box body (55), the second rotating hydraulic cylinder (56) drives the brush wires (12) to rotate and stretch through the first circular plate (11), so that the brush wires (12) clear the inner wall of the hollow tube (5), and the rotary table (4) is restored to the original position after clearing, so that the hollow tube (5) is kept clean all the time;
s3, moving the small stirring boxes (41) which are not filled with materials to the hollow tubes (5) through a first servo motor (31), after moving, putting linolenic acid and stannous octoate into one group of small stirring boxes (41) through the hollow tubes (5), and after, putting a thickening agent and a preservative into the other group of small stirring boxes (41) through the other group of hollow tubes (5);
s4, after materials are filled in the small stirring box (41), the rotary table (4) is driven to rise through the first hydraulic cylinder (33) until the rotary table (4) is attached to the round cover plate (22), and after the rotary table is attached, the U-shaped heating pipe (23) is started until the temperature in the small stirring box (41) reaches the temperature required by the materials, wherein the temperature of the emulsified silicone oil and the organosilicon is 150 ℃, the temperature of the modified silicon polyether and the high-carbon alcohol fatty acid ester compound is 120 ℃, the temperature of the linolenic acid and the stannous octoate is 130 ℃, and the temperature of the thickener and the preservative is 90 ℃;
s5, then servo motor two (412) will drive agitator one (414) and rotate, rotatory agitator one (414) will stir the mixture to the material, when stirring the mixture to the material back, will turn round platform (4) and resume the normal position, nevertheless will take out little agitator tank (41) from revolving platform (4), after taking out, pour the mixed material in little agitator tank (41) into big agitator tank (42), after pouring, go on rising revolving platform (4) until big agitator tank (42) laminating circular apron (22), then start U type heating pipe (23) again, until make the temperature in the big agitator tank 42 reach 130 ℃, then servo motor three (422) will drive agitator two (424) and rotate, rotatory agitator two (424) will stir the mixture to multiunit mixed material.
2. The process of a high temperature resistant defoamer of claim 1, wherein: the cleaning device (1) further comprises a second circular plate (13), the output end of the second hydraulic cylinder (56) is inserted into the inner wall of the second circular plate (13), and the second circular plate (13) is inserted into the inner wall of the sponge (14).
3. The process of a high temperature resistant defoamer of claim 1, wherein: the novel heating box is characterized in that support columns (21) are fixedly mounted at two ends of the inner wall of the top of the large box body (2), a round cover plate (22) is fixedly mounted at the bottom of the support columns (21), a U-shaped heating pipe (23) is fixedly mounted at the bottom of the round cover plate (22), and at least one group of U-shaped heating pipes (23) are arranged.
4. The process of a high temperature resistant defoamer of claim 1, wherein: the first box body (3) is fixedly arranged at the bottom of the large box body (2).
5. The process of a high temperature resistant defoamer of claim 1, wherein: the two ends of the inner wall of the large box body (2) are inserted with the hollow tubes (5).
6. The process of a high temperature resistant defoamer of claim 1, wherein: the inner wall of the top end of the hollow tube (5) is provided with a feed inlet (51).
7. The process of a high temperature resistant defoamer of claim 1, wherein: the small stirring box (41) and the large stirring box (42) are positioned below the U-shaped heating pipe (23).
8. The process of a high temperature resistant defoamer of claim 1, wherein: the output end of the hollow pipe (5) is positioned above the small stirring box (41).
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