CN112742072A - 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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- CN112742072A CN112742072A CN202011481802.0A CN202011481802A CN112742072A CN 112742072 A CN112742072 A CN 112742072A CN 202011481802 A CN202011481802 A CN 202011481802A CN 112742072 A CN112742072 A CN 112742072A
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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 particularly relates to the technical field of defoaming agents, wherein the technical scheme is as follows: the beverage comprises main materials and auxiliary materials, wherein the main materials (by weight) comprise: emulsified silicone oil: 15g-20g, silicone: 20g-30g, modified silicon polyether: 20g-35g, higher alcohol fatty acid ester complex: 10g-15g, linolenic acid: 6g-12g, stannous octoate: 6g-8g, wherein the auxiliary materials (by weight) comprise a thickening agent: 10g-20g, preservative: 5g-10g, comprising a cleaning device, a large box body, a box body I, a rotating platform and a hollow pipe, wherein a servo motor I is fixedly arranged on the inner wall of the box body I, and the output end of the servo motor I is inserted into the inner wall of the box body I, the invention has the beneficial effects that: through when separating multiunit material, still stir simultaneously and mix, mix the back, stir the multiunit mixed material again and mix, so not only save time, still improved output and reduced the input of cost.
Description
Technical Field
The invention relates to the field of defoaming agents, and particularly relates to a high-temperature-resistant defoaming agent, a production line and a process.
Background
The defoaming agent, also called defoaming agent, is a food additive for reducing surface tension in the food processing process, inhibiting foam generation or eliminating foam generated, the defoaming agent permitted in China includes 7 kinds of emulsified silicone oil, higher alcohol fatty acid ester compound, polyoxyethylene polyoxypropylene pentaerythritol ether, polyoxyethylene polyoxypropylene amine ether, polyoxypropylene glycerol ether, polyoxypropylene polyoxyethylene glycerol ether, polydimethylsiloxane and the like, the defoaming agent is also called antifoaming agent, a lot of harmful foams can be generated in the industrial production process, the defoaming agent needs to be added, the defoaming agent is widely applied to eliminating harmful foams generated in the industrial production processes of latex, textile sizing, food fermentation, biomedicine, pesticide, coating, petrochemical industry, papermaking, industrial cleaning and the like, and the defoaming agent needs to stir and mix a plurality of materials in sequence during production.
The prior art has the following defects: the existing stirring device generally needs to clean the stirring device firstly after stirring and mixing a group of materials and then stir the next group of materials, so that not only is the time wasted, but also the yield of the defoaming agent is reduced.
Therefore, the invention is necessary to invent a high-temperature resistant defoaming agent, 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 corresponding small stirring box is moved to a hollow pipe through a rotating rotary table, then the hollow pipe can flow corresponding materials into the small stirring box, and then the hollow pipe is cleaned through a cleaning device, so that the problem that after one group of materials are stirred and mixed, the stirring device needs to be cleaned first and then the next group of materials needs to be stirred by the conventional stirring device is solved.
In order to achieve the above purpose, the invention provides the following technical scheme: the high-temperature-resistant defoaming agent comprises main materials and auxiliary materials, wherein the main materials comprise (by weight): emulsified silicone oil: 15g-20g, silicone: 20g-30g, modified silicon polyether: 20g-35g, higher alcohol fatty acid ester complex: 10g-15g, linolenic acid: 6g-12g, stannous octoate: 6g-8g, wherein the auxiliary materials (by weight) comprise a thickening agent: 10g-20g, preservative: 5g to 10 g.
A high-temperature-resistant defoaming agent production line comprises a cleaning device, a large box body, a box body I, a rotating table and a hollow pipe, wherein a servo motor I is fixedly installed on the inner wall of the box body I, an output end of the servo motor I is inserted into the inner wall of the box body I, a hydraulic cylinder I is fixedly installed on the inner wall of the box body I, and an output end of the hydraulic cylinder I is inserted into the inner wall of the rotating table;
the inner wall of the top end of the rotating table is arranged in a square shape and is in threaded connection with a small stirring box, a first partition plate is inserted into the inner wall of the bottom end of the small stirring box, a second box body is fixedly installed on the inner wall of the bottom end of the small stirring box, a second servo motor is fixedly installed on the inner wall of the second box body, and the output end of the second servo motor penetrates through the first partition plate and is inserted into the inner wall of the first;
the inner wall of the middle end of the top of the rotating table is in threaded connection with a large stirring box, a second partition plate is inserted into the inner wall of the bottom end of the large stirring box, a third box body is fixedly installed on the inner wall of the bottom end of the large stirring box, a third servo motor is fixedly installed on the inner wall of the third box body, and the output end of the third servo motor penetrates through the second partition plate and is inserted into the inner wall of the second stirrer;
one end of the inner wall of the hollow pipe is inserted with a baffle, one end of the outer wall of the baffle is fixedly provided with a box body IV, the inner wall of the box body IV is fixedly provided with a servo motor IV, the output end of the servo motor IV penetrates through the baffle to be inserted into the inner wall of the box body II, and the inner wall of the box body II is fixedly provided with a hydraulic cylinder II;
the cleaning device comprises a first circular plate, the output end of the second hydraulic cylinder 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, support columns are fixedly installed at two ends of the inner wall of the top of the large box body, a circular cover plate is fixedly installed at the bottom of each support column, U-shaped heating pipes are fixedly installed at the bottom of each circular cover plate, and the U-shaped heating pipes are at least one group.
Preferably, the first box body is fixedly installed at the bottom of the large box body.
Preferably, the hollow pipe is inserted at two ends of the inner wall of the large box body.
Preferably, the inner wall of the top end of the hollow pipe is provided with a feeding hole.
Preferably, the small stirring box and the large stirring box are positioned below the U-shaped heating pipe.
Preferably, the output end of the hollow pipe is positioned above the small stirring box.
A high-temperature resistant defoaming agent process further comprises the following specific steps:
s1, starting a first servo motor, driving a first hydraulic cylinder to rotate by the first servo motor through a first box body, driving a rotating platform to rotate by the first hydraulic cylinder until the rotating platform moves one group of small stirring boxes to the hollow pipe, putting emulsified silicone oil and organic silicon into the hollow pipe through a feeding hole, allowing the materials to flow into the small stirring boxes, and putting the modified silicon polyether and high-carbon alcohol fatty acid ester compound into another group of small stirring boxes through another group of hollow pipes;
s2, when the materials flow into the small stirring box, the hydraulic cylinder I drives the rotating platform to ascend until the rotating platform is higher than the hollow pipe, then the servo motor II drives the hydraulic cylinder II to rotate through the box body II, the rotating hydraulic cylinder II drives the brush wires to rotate and stretch through the circular plate I, so that the brush wires clean the inner wall of the hollow pipe, and the rotating platform is restored to the original position after cleaning, so that the hollow pipe can be kept clean all the time;
s3, moving the small stirring boxes in which the materials are not filled to the hollow pipes through the first servo motor, putting linolenic acid and stannous octoate into one group of small stirring boxes through the hollow pipes after moving, and putting the thickening agent and the preservative into the other group of small stirring boxes through the other group of hollow pipes;
s4, after the materials are filled in the small stirring box, the hydraulic cylinder drives the rotating platform to ascend until the rotating platform is attached to the circular cover plate, and after the materials are attached, the 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 organic silicon is 150 ℃, the temperature of a modified silicon polyether and high 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, then the servo motor II drives the stirrer I to rotate, the rotating stirrer I stirs and mixes materials, after the materials are stirred and mixed, the rotating platform is restored to the original position, then the small stirring box is taken out of the rotating platform, after the materials are taken out, the mixed materials in the small stirring box are poured into the large stirring box, after the materials are poured, the rotating platform is lifted until the large stirring box is attached to the circular cover plate, then the U-shaped heating pipe is started until the temperature in the large stirring box reaches 130 ℃, then the servo motor III drives the stirrer II to rotate, and the rotating stirrer II stirs and mixes a plurality of groups of mixed materials.
The invention has the beneficial effects that:
when the invention is used, the servo motor drives the first hydraulic cylinder to rotate through the first box body, then the first hydraulic cylinder drives the rotating platform to rotate until the rotating platform moves the corresponding small stirring box to the hollow pipe, then the corresponding material is placed in the hollow pipe through the feed inlet, then the material flows into the small stirring box, when the material flows into the small stirring box, the first hydraulic cylinder drives the rotating platform to ascend until the rotating platform is higher than the hollow pipe, then the servo motor drives the second hydraulic cylinder to rotate through the second box body, the second rotating hydraulic cylinder drives the brush wires to rotate and stretch through the first circular plate, so that the brush wires clean the inner wall of the hollow pipe, the rotating platform is restored to the original position after cleaning, so that the hollow pipe is kept clean all the time, the quality of the defoaming agent is improved, when the material is placed into the corresponding small stirring box, the rotating table is driven to ascend through the first hydraulic cylinder again until the rotating table is attached to the circular cover plate, after the materials are attached to the rotating table, the U-shaped heating pipe is started until the temperature in the small stirring box reaches the temperature required by the materials, then the first servo motor drives the first stirrer to rotate, the rotating first stirrer stirs and mixes the materials, after the materials are stirred and mixed, the rotating table is restored to the original position, then the small stirring box is taken out of the rotating table, after the materials are taken out, the mixed materials in the small stirring box are poured into the large stirring box, after the materials are poured, the rotating table is ascended until the large stirring box is attached to the circular cover plate, then the U-shaped heating pipe is started until the temperature in the large stirring box reaches the temperature required by the mixed materials, then the third servo motor drives the second stirrer to rotate, and the second rotating stirrer stirs and mixes a plurality of groups of mixed materials, through when separating multiunit material, still stir simultaneously and mix, mix the back, stir the multiunit mixed material again and mix, so not only save time, still improved output and reduced the input of cost.
Drawings
FIG. 1 is a schematic front view of the structure of embodiment 1 provided by the present invention;
FIG. 2 is a schematic top view of the structure of example 1 provided in the present invention;
FIG. 3 is an enlarged schematic view of the front view area A of the structure of embodiment 1 provided by the present invention;
FIG. 4 is an enlarged schematic view of the front view B region of the structure of embodiment 1 provided by the present invention;
FIG. 5 is an enlarged schematic view of the front view C region of the structure of embodiment 1 provided by the present invention;
FIG. 6 is an enlarged schematic view of the front view D area of the structure of embodiment 1 provided by the present invention;
FIG. 7 is a schematic front view of the structure of embodiment 2 provided by the present invention;
fig. 8 is an enlarged schematic view of the front view E area of the structure of embodiment 2 provided by the present invention.
In the figure: the cleaning device comprises a cleaning device 1, a first circular plate 11, a brush wire 12, a second circular plate 13, a sponge 14, a large box 2, a support column 21, a circular cover plate 22, a U-shaped heating pipe 23, a first box 3, a first servo motor 31, a first box 32, a first hydraulic cylinder 33, a rotary table 4, a small stirring box 41, a second box 411, a second servo motor 412, a first partition 413, a first stirrer 414, a large stirring box 42, a third box 421, a third servo motor 422, a second partition 423, a second stirrer 424, a hollow pipe 5, a feed inlet 51, a fourth box 52, a fourth servo motor 53, a baffle 54, a second box 55 and a second hydraulic cylinder 56.
Detailed Description
The preferred embodiments of the present invention will be described in conjunction with the accompanying drawings, and it will be understood that they are described herein for the purpose of illustration and explanation and not limitation.
The high-temperature-resistant defoaming agent comprises main materials and auxiliary materials, wherein the main materials comprise (by weight): emulsified silicone oil: 15g-20g, silicone: 20g-30g, modified silicon polyether: 20g-35g, higher alcohol fatty acid ester complex: 10g-15g, linolenic acid: 6g-12g, stannous octoate: 6g-8g, wherein the auxiliary materials (by weight) comprise a thickening agent: 10g-20g, preservative: 5g to 10 g.
further, a 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, a 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 rotating platform 4, specifically, the first servo motor 31 is an engine which controls mechanical elements to operate in a servo system and is an indirect speed change device of a supplementary motor, the first servo motor 31 is set to be 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 executive component which converts hydraulic energy into mechanical energy and makes linear reciprocating motion or swinging motion, the first hydraulic cylinder 33 is set to be CDM1, the first hydraulic cylinder 33 has the function of driving the rotating platform 4 to rotate and lift, the rotating platform 4 has the function of moving a corresponding, the elevated rotary table 4 has a function of closing the small agitation tank 41 and the large agitation tank 42 by the circular cover 22.
Further, the inner wall of the top end of the rotating platform 4 is in a square arrangement and is in threaded connection with the small stirring boxes 41, the inner wall of the bottom end of each small stirring box 41 is inserted with a first partition plate 413, the inner wall of the bottom end of each small stirring box 41 is fixedly provided with a second box body 411, the inner wall of the second box body 411 is fixedly provided with a 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 an effect of preventing materials from flowing into the bottom end of each small stirring box 41, the second servo motor 412 is set to be SM 80-013-30LFB, the second servo motor 412 has an effect of driving the first stirrer 414 to rotate, and the first.
Further, the inner wall of the middle end of the top of the rotating platform 4 is in threaded connection with a large stirring box 42, the inner wall of the bottom end of the large stirring box 42 is inserted with a second partition plate 423, the inner wall of the bottom end of the large stirring box 42 is fixedly provided with a third box 421, the inner wall of the third box 421 is fixedly provided with a third servo motor 422, the output end of the third servo motor 422 penetrates through the second partition plate 423 to be inserted into the inner wall of the second stirrer 424, specifically, the second partition plate 423 has an effect of preventing the mixed materials from flowing into the bottom end of the large stirring box 42, the third servo motor 422 is set to be SM 110-.
Further, a baffle 54 is inserted into one end of the inner wall of the hollow tube 5, a box body four 52 is fixedly mounted at one end of the outer wall of the baffle 54, a servo motor four 53 is fixedly mounted on the inner wall of the box body four 52, the output end of the servo motor four 53 penetrates through the baffle 54 and is inserted into the inner wall of a box body two 55, a hydraulic cylinder two 56 is fixedly mounted on the inner wall of the box body two 55, specifically, the hollow tube 5 has the function of material flowing, the baffle 54 has the fixing function on the box body four 52, the servo motor four 53 is set to be SM 150-25LFB, the servo motor four 53 has the function of driving the hydraulic cylinder two 56 to rotate through the box body two 55, and the hydraulic cylinder two 56.
Further, the cleaning device 1 comprises a first circular plate 11, the output end of a second hydraulic cylinder 56 is connected to the inner wall of the first circular plate 11 in an inserting mode, brush wires 12 are arranged on the circumference of the outer wall of the first circular plate 11, specifically, the second hydraulic cylinder 56 has the function of driving the first circular plate 11 to rotate and stretch, the first circular plate 11 has the function of driving the brush wires 12 to rotate and stretch, and the brush wires 12 have the function of cleaning the inner wall of the hollow pipe 5.
Further, 2 top inner wall both ends fixed mounting support columns 21 of big box, the circular apron 22 of support column 21 bottom fixed mounting, circular apron 22 bottom fixed mounting U type heating pipe 23, U type heating pipe 23 is a set of at least, and is concrete, and circular apron 22 has and lets little agitator tank 41 and big agitator tank 42 carry out the closed effect to prevent that the material from flowing out, U type heating pipe 23 has and carries out the effect that improves to the temperature in little agitator tank 41 and the big agitator tank 42, and U type heating pipe 23 is preferred to be five groups.
Further, the first box body 3 is fixedly installed at the bottom of the large box body 2, and specifically, the large box body 2 has a fixing effect on the first box body 3.
Further, the hollow tube 5 is inserted at 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 tube 5.
Further, the inner wall of the top end of the hollow tube 5 is provided with a feed inlet 51, and particularly, the feed inlet 51 has the function of placing materials in the hollow tube 5.
Further, the small stirring box 41 and the large stirring box 42 are located below the U-shaped heating pipe 23, and specifically, the small stirring box 41 and the large stirring box 42 are located below the U-shaped heating pipe 23, which has an effect of facilitating the increase of the temperature in the small stirring box 41 and the large stirring box 42.
Further, the output end of the hollow pipe 5 is positioned above the small stirring box 41, and particularly, the output end of the hollow pipe 5 is positioned above the small stirring box 41, so that the material can be conveniently flowed into the small stirring box 41.
The using 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 rotating platform 4 to rotate until the rotating platform 4 moves one group of small stirring boxes 41 to the hollow pipe 5, and then the emulsified silicone oil: 15g to 20g, preferably 17.5g and silicone: 20g to 30g, preferably 25g, are placed in the hollow tube 5 through the inlet 51, the material then flows into the small stirring box 41, after which the modified silicon polyether: 20g to 35g, preferably 27.5g and higher alcohol fatty acid ester complex: 10g-15g, preferably 12.5g, put into another group of little agitator tank 41 through another group of hollow tube 5, when the material flowed into little agitator tank 41, hydraulic cylinder 33 will drive revolving stage 4 and rise until revolving stage 4 is higher than hollow tube 5, then servo motor four 53 will drive hydraulic cylinder two 56 through box body two 55 and rotate, rotatory hydraulic cylinder two 56 will drive brush silk 12 through first disk 11 and rotate and stretch out and draw back, thereby make brush silk 12 clear up the 5 inner walls of hollow tube, resume the normal position with revolving stage 4 after the clearance, will make hollow tube 5 keep clean constantly like this, then make the little agitator tank 41 that does not pack into the material move to hollow tube 5 department through servo motor one 31, move to the back, with linolenic acid: 6g to 12g, preferably 9g and stannous octoate: 6g to 8g, preferably 7g, are placed through the hollow tube 5 into one of the small mixing tanks 41, after which the thickener: 10g to 20g, preferably 15g and preservatives are used: 5g-10g, preferably 7.5g, is placed into another group of small stirring boxes 41 through another group of hollow pipes 5, after materials are all loaded into the small stirring boxes 41, the rotating platform 4 is driven by a hydraulic cylinder 33 to ascend until the rotating platform 4 is attached to the circular cover plate 22, after the materials are attached, the 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 emulsified silicone oil and organic silicon is 150 ℃, the temperature of a modified silicone 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 ℃, then a servo motor II 412 drives a stirrer I414 to rotate, the rotating stirrer I414 stirs and mixes the materials, and after the materials are stirred and mixed, the rotating platform 4 is restored to the original position, the small stirring box 41 is taken out of the rotating platform 4, after the small stirring box 41 is taken out, the mixed materials in the small stirring box 41 are poured into the large stirring box 42, after the mixed materials are poured, the rotating platform 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 ℃, then the third servo motor 422 drives the second stirrer 424 to rotate, the second rotary stirrer 424 stirs and mixes a plurality of 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.
further, the cleaning device 1 further comprises a circular plate II 13, the output end of the hydraulic cylinder II 56 is connected with the inner wall of the circular plate II 13 in an inserting mode, the circular plate II 13 is connected with the inner wall of the sponge 14 in an inserting mode, specifically, the hydraulic cylinder II 56 has the function of driving the circular plate II 13 to rotate and stretch, the circular plate II 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 pipe 5.
The using 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 rotating platform 4 to rotate until the rotating platform 4 moves one group of small stirring boxes 41 to the hollow pipe 5, and then the emulsified silicone oil: 15g to 20g, preferably 17.5g and silicone: 20g to 30g, preferably 25g, are placed in the hollow tube 5 through the inlet 51, the material then flows into the small stirring box 41, after which the modified silicon polyether: 20g to 35g, preferably 27.5g and higher alcohol fatty acid ester complex: 10g-15g, preferably 12.5g, put into another group of little agitator tank 41 through another group of hollow tube 5, when the material flowed into little agitator tank 41, hydraulic cylinder 33 will drive revolving stage 4 and rise until revolving stage 4 is higher than hollow tube 5, then servo motor four 53 will drive hydraulic cylinder two 56 through box body two 55 and rotate, rotatory hydraulic cylinder two 56 will drive sponge 14 through two 13 plectanes and rotate and stretch, thereby make sponge 14 clear up the 5 inner walls of hollow tube, resume the normal position with revolving stage 4 after the clearance, will make hollow tube 5 keep clean constantly like this, then make the little agitator tank 41 that does not pack into the material move to hollow tube 5 department through servo motor one 31, move to the back, with linolenic acid: 6g to 12g, preferably 9g and stannous octoate: 6g to 8g, preferably 7g, are placed through the hollow tube 5 into one of the small mixing tanks 41, after which the thickener: 10g to 20g, preferably 15g and preservatives are used: 5g-10g, preferably 7.5g, is placed into another group of small stirring boxes 41 through another group of hollow pipes 5, after materials are all loaded into the small stirring boxes 41, the rotating platform 4 is driven by a hydraulic cylinder 33 to ascend until the rotating platform 4 is attached to the circular cover plate 22, after the materials are attached, the 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 emulsified silicone oil and organic silicon is 150 ℃, the temperature of a modified silicone 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 ℃, then a servo motor II 412 drives a stirrer I414 to rotate, the rotating stirrer I414 stirs and mixes the materials, and after the materials are stirred and mixed, the rotating platform 4 is restored to the original position, then, the small stirring box 41 is taken out of the rotating platform 4, after the small stirring box 41 is taken out, the mixed materials in the small stirring box 41 are poured into the large stirring box 42, after the mixed materials are poured, the rotating platform 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 ℃, then the second stirrer 424 is driven by the third servo motor 422 to rotate, the second rotary stirrer 424 can stir and mix a plurality of groups of mixed materials, wherein the inner wall of the hollow pipe 5 is cleaned by the sponge 14, and the effect of preventing the inner wall of the hollow pipe 5 from generating scratches is achieved.
Example 3:
a high-temperature resistant defoaming agent process further comprises the following specific steps:
s1, starting the first servo motor 31, driving the first servo motor 31 to drive the first hydraulic cylinder 33 to rotate through the first box body 32, then driving the rotary table 4 to rotate through the first hydraulic cylinder 33 until the rotary table 4 moves one group of small stirring boxes 41 to the hollow pipe 5, then placing emulsified silicone oil and organic silicon in the hollow pipe 5 through the feed inlet 51, then enabling the materials to flow into the small stirring boxes 41, and then placing the modified silicon polyether and high-carbon alcohol fatty acid ester compound in the other group of small stirring boxes 41 through the other group of hollow pipes 5;
s2, when the materials flow into the small stirring box 41, the first hydraulic cylinder 33 drives the rotating platform 4 to ascend until the rotating platform 4 is higher than the hollow pipe 5, then the servo motor IV 53 drives the second hydraulic cylinder 56 to rotate through the box body II 55, the second rotating hydraulic cylinder 56 drives the brush wires 12 to rotate and stretch through the circular plate I11, so that the brush wires 12 clean the inner wall of the hollow pipe 5, and the rotating platform 4 is restored to the original position after cleaning, so that the hollow pipe 5 is kept clean all the time;
s3, moving the small stirring boxes 41 which are not filled with materials to the hollow pipes 5 through the first servo motor 31, then putting linolenic acid and stannous octoate into one group of small stirring boxes 41 through the hollow pipes 5, and then putting the thickening agent and the preservative into the other group of small stirring boxes 41 through the other group of hollow pipes 5;
s4, after materials are filled in the small stirring box 41, the rotating platform 4 is driven to ascend through the hydraulic cylinder I33 until the rotating platform 4 is attached to the circular cover plate 22, after the materials are 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 emulsified silicone oil and organic silicon 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 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 rotating platform 4 is restored to the original position, the small stirring box 41 is taken out of the rotating platform 4, after the materials are taken out, the mixed materials in the small stirring box 41 are poured into the large stirring box 42, after the materials are poured, the rotating platform 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 ℃, then the third servo motor 422 drives the second stirrer 424 to rotate, and the second rotating stirrer 424 stirs and mixes a plurality of groups of mixed materials.
The above description is only a preferred embodiment of the present invention, and any person skilled in the art may modify the present invention or modify it into an equivalent technical solution by using the technical solution described above. Therefore, any simple modifications or equivalent substitutions made in accordance with the technical solution of the present invention are within the scope of the claims of the present invention.
Claims (10)
1. The high-temperature-resistant defoaming agent comprises main materials and auxiliary materials, and is characterized in that: the main materials (by weight) comprise: emulsified silicone oil: 15g-20g, silicone: 20g-30g, modified silicon polyether: 20g-35g, higher alcohol fatty acid ester complex: 10g-15g, linolenic acid: 6g-12g, stannous octoate: 6g-8g, wherein the auxiliary materials (by weight) comprise a thickening agent: 10g-20g, preservative: 5g to 10 g.
2. The utility model provides a high temperature resistant defoaming agent production line, includes belt cleaning device (1), big box (2), box (3), revolving stage (4) and hollow tube (5), its characterized in that: a 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), a first hydraulic cylinder (33) is fixedly installed on the inner wall of the first box body (32), and the output end of the first hydraulic cylinder (33) is inserted into the inner wall of the rotating table (4);
the inner wall of the top end of the rotating platform (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 installed on the inner wall of the bottom end of the small stirring box (41), a second servo motor (412) is fixedly installed 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 rotating platform (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 body (421) is fixedly installed on the inner wall of the bottom end of the large stirring box (42), a third servo motor (422) is fixedly installed on the inner wall of the third box body (421), and the output end of the third servo motor (422) penetrates through the second partition plate (423) to be inserted into the inner wall of the second stirrer (424);
a baffle (54) is inserted at one end of the inner wall of the hollow pipe (5), a box body IV (52) is fixedly installed at one end of the outer wall of the baffle (54), a servo motor IV (53) is fixedly installed on the inner wall of the box body IV (52), the output end of the servo motor IV (53) penetrates through the baffle (54) to be inserted into the inner wall of the box body II (55), and a hydraulic cylinder II (56) is fixedly installed on the inner wall of the box body II (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).
3. The high temperature resistant defoamer production line of claim 2, 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).
4. The high temperature resistant defoamer production line of claim 2, wherein: big box (2) top inner wall both ends fixed mounting support column (21), support column (21) bottom fixed mounting circular cover plate (22), circular cover plate (22) bottom fixed mounting U type heating pipe (23), U type heating pipe (23) are a set of at least.
5. The high temperature resistant defoamer production line of claim 2, wherein: the first box body (3) is fixedly installed at the bottom of the large box body (2).
6. The high temperature resistant defoamer production line of claim 2, wherein: the hollow pipe (5) is inserted at two ends of the inner wall of the large box body (2).
7. The high temperature resistant defoamer production line of claim 2, wherein: the inner wall of the top end of the hollow pipe (5) is provided with a feeding hole (51).
8. The high temperature resistant defoamer production line of claim 2, wherein: the small stirring box (41) and the large stirring box (42) are positioned below the U-shaped heating pipe (23).
9. The high temperature resistant defoamer production line of claim 2, wherein: the output end of the hollow pipe (5) is positioned above the small stirring box (41).
10. A high-temperature resistant defoaming agent process is characterized in that: the method also comprises the following specific steps:
s1, starting a first servo motor (31), wherein the first servo motor (31) drives a first hydraulic cylinder (33) to rotate through a first box body (32), then the first hydraulic cylinder (33) drives a rotary table (4) to rotate until the rotary table (4) moves one group of small stirring boxes (41) to the hollow pipe (5), then emulsified silicone oil and organic silicon are placed in the hollow pipe (5) through a feeding hole (51), then the materials flow into the small stirring boxes (41), and after the materials pass through the small stirring boxes, the modified silicone polyether and high-carbon alcohol fatty acid ester compound is placed in the other group of small stirring boxes (41) through the other group of hollow pipes (5);
s2, when the materials flow into the small stirring box (41), the first hydraulic cylinder (33) drives the rotating platform (4) to ascend until the rotating platform (4) is higher than the hollow pipe (5), then the servo motor IV (53) drives the second hydraulic cylinder (56) to rotate through the box body II (55), the rotating second hydraulic cylinder (56) drives the brush wire (12) to rotate and stretch through the circular plate I (11), so that the brush wire (12) cleans the inner wall of the hollow pipe (5), and the rotating platform (4) is restored to the original position after cleaning, so that the hollow pipe (5) is kept clean all the time;
s3, moving the small stirring boxes (41) which are not filled with materials to the hollow pipes (5) through the servo motor I (31), putting linolenic acid and stannous octoate into one group of small stirring boxes (41) through the hollow pipes (5), and then putting the thickening agent and the preservative into the other group of small stirring boxes (41) through the other group of hollow pipes (5);
s4, after materials are filled in the small stirring box (41), driving the rotating platform (4) to ascend through the hydraulic cylinder I (33) until the rotating platform (4) is attached to the circular cover plate (22), and starting the U-shaped heating pipe (23) until the temperature in the small stirring box (41) reaches the temperature required by the materials, wherein the temperature of emulsified silicone oil and organic silicon 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 (414) is driven by the second servo motor (412) to rotate, the first rotating stirrer (414) is used for stirring and mixing materials, after the materials are stirred and mixed, the rotating platform (4) is restored to the original position, the small stirring box (41) is taken out of the rotating platform (4), after the materials are taken out, the mixed materials in the small stirring box (41) are poured into the large stirring box (42), after the materials are poured, the rotating platform (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 ℃, then the second stirrer (424) is driven by the third servo motor (422) to rotate, and the second rotating stirrer (424) is used for stirring and mixing multiple groups of mixed materials.
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