CN112076638A - Simple sludge slurrying system and method - Google Patents
Simple sludge slurrying system and method Download PDFInfo
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- CN112076638A CN112076638A CN202010965347.5A CN202010965347A CN112076638A CN 112076638 A CN112076638 A CN 112076638A CN 202010965347 A CN202010965347 A CN 202010965347A CN 112076638 A CN112076638 A CN 112076638A
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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
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/60—Pump mixers, i.e. mixing within a pump
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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
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/40—Static mixers
- B01F25/42—Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions
- B01F25/43—Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction
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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
- B01F35/20—Measuring; Control or regulation
- B01F35/21—Measuring
- B01F35/213—Measuring of the properties of the mixtures, e.g. temperature, density or colour
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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
- B01F35/20—Measuring; Control or regulation
- B01F35/21—Measuring
- B01F35/2132—Concentration, pH, pOH, p(ION) or oxygen-demand
Abstract
The invention relates to a simple sludge slurrying system and a simple sludge slurrying method, wherein the simple sludge slurrying system comprises a raw material pump which is arranged on a base platform through a support, a water injection port is formed in a feed inlet above the raw material pump, a pipeline and an elbow are arranged on one side of the raw material pump, the outlet of the elbow is connected with a turbulator, a power source and a speed changer are arranged on the other side of the raw material pump, an output shaft of the power source is connected with a stirring device in the raw material pump through the speed changer, and the outer side of the power source; the concentration, the particle size and the flow parameter of the mixed sludge detected by the sampling detection port are adjusted according to the adjustment requirement, the adjustment mode and the adjustment priority determined in the priority adjustment unit, the parameter adjustment of the position of the water injection port, the adjustment of the corresponding parameter of the stirring device and the corresponding adjustment of the corresponding parameter of the pipeline and the elbow are realized, so that the efficiency and the accuracy of sludge mixing and slurrying are effectively improved, and meanwhile, the further improvement of a slurrying system and a slurrying method is further realized through continuous optimization.
Description
Technical Field
The invention relates to the technical field of environment-friendly treatment of urban sewage and sludge, in particular to a simple sludge slurrying system and method.
Background
With the development of society, the kitchen waste is more and more passed over, and whether the kitchen waste can be properly disposed, so that the problems of food sanitation and safety and the health of people are directly involved; meanwhile, with the rapid development of the urban sewage treatment industry in China, the sludge production amount is increasing day by day. The patent 'a kitchen waste and sewage plant sludge cooperative treatment method' (application publication No. CN106964633A, publication No. 2017.07.21) discloses a kitchen waste and sewage plant sludge cooperative treatment method, which can not only stably treat kitchen waste and domestic sludge to make the kitchen waste and the domestic sludge harmless and reduced, but also produce available methane and garden biological carbon soil to change waste into valuable.
In the prior art, the concentration of sludge fed is about 80% of water content, and the sludge can enter a thermal hydrolysis tank only after being modified to 90% by a slurrying process, and then the next process is continued. The process flow needs a hopper, a sludge raw material pump, a spiral pulpifying machine, a pulpifying machine water tank, a pulpifying machine middle storage bin, a sludge conveying pump, a valve instrument and other equipment, and has high manufacturing cost and complex operation process. Meanwhile, in the slurrying process, each parameter cannot be effectively and accurately controlled in a targeted manner according to the detection result after slurrying, so that the accuracy and the slurrying efficiency of slurried sludge are influenced.
Disclosure of Invention
In order to overcome the defects in the prior art, the invention provides a simple sludge slurrying system and a simple sludge slurrying method.
The technical scheme adopted by the invention for solving the technical problems is as follows:
the utility model provides a simple and easy sludge slurrying system, includes through the former pump of support mounting on the base station, has seted up the water filling port on the top feed inlet of former pump, is provided with pipeline and elbow in one side of former pump, and the export and the turbulator of elbow are connected, are provided with power supply and derailleur at the opposite side of former pump, and the output shaft of power supply is connected with the inside agitating unit of former pump through the derailleur, and the outside of power supply still is connected with controller, its characterized in that:
the aperture of the opening of the water injection port, the inclination angle and the water injection temperature can be adjusted in real time through the controller;
the number of the stirring blades of the stirring device, the extending radius of the stirring blades and the rotating speed of the stirring blades can be adjusted in real time through the controller;
mud resistance areas extend out of the inner walls of the pipeline and the elbow, and the number and the area of the mud resistance areas and the corner angle of the elbow can be adjusted in real time through a controller;
the turbulator is provided with a sampling detection port, a priority adjusting unit is arranged in the controller, and the controller realizes corresponding adjustment according to detection data of the sampling detection port and according to adjustment requirements, adjustment modes and adjustment priorities determined in the priority adjusting unit.
Furthermore, the detection data of the sampling detection port at least comprises concentration detection data, particle size detection data and flow detection data.
Further, the preset regulation requirements in the priority regulation unit satisfy:
Y＝aY1+bY2+cY3 (1)
wherein the content of the first and second substances,
y represents a regulation demand value determined in the priority regulation unit;
y0 represents a regulation demand value preset in the priority regulation unit;
when Y is more than Y0, starting the controller to realize corresponding adjustment; when Y is less than Y0, the controller is not started to realize corresponding adjustment;
a represents a sludge concentration coefficient;
b represents a sludge particle size coefficient;
c represents a sludge flow coefficient;
y1 represents a deviation value of sludge concentration and satisfies
Y1＝|X1-X10|/X10 (2)
Wherein the content of the first and second substances,
x1 represents an actual measurement value of the sludge concentration,
x10 denotes a preset sludge concentration value;
y2 represents a deviation value of sludge particle size and satisfies
Y2＝|X2-X20|/X20 (3)
Wherein the content of the first and second substances,
x2 represents an actual measurement value of the sludge particle diameter,
x20 represents a preset value of sludge particle size;
y3 represents a deviation value of the sludge flow rate and satisfies
Y3＝|X3-X30|/X30 (4)
Wherein the content of the first and second substances,
x3 represents the measured value of the sludge flow rate,
x30 represents a preset sludge flow rate value;
further, the priority adjusting unit sorts the sludge concentration deviation value Y1, the sludge particle size deviation value Y2 and the sludge flow deviation value Y3 in sequence, and selects a preset adjusting mode corresponding to the maximum value as the adjusting mode of the current controller.
Furthermore, the preset adjusting mode of the sludge concentration deviation value Y1 in the controller is to preferentially adjust the opening aperture, the inclination angle and the water injection temperature of the water injection port in real time, then adjust the number and the area of mud resistance areas extending out of the inner walls of the pipeline and the elbow and the corner radius of the elbow in real time, and finally adjust the number of stirring blades of the stirring device, the extending radius of the stirring blades and the rotating speed of the stirring blades in real time;
the preset adjusting mode of the controller for the sludge particle size deviation value Y2 is to perform preferential real-time adjustment on the number of stirring blades of the stirring device, the extension radius of the stirring blades and the rotating speed of the stirring blades, then perform real-time adjustment on the number and area of mud resistance areas extending out of the inner walls of the pipeline and the elbow and the corner radius of the elbow, and finally perform preferential real-time adjustment on the opening aperture, the inclination angle and the water injection temperature of the water injection port;
the regulation mode that predetermines mud flow deviation value Y3 in the controller is right the mud that the inner wall of pipeline and elbow stretches out the setting hinders regional quantity, area and the corner radius of elbow carries out preferential real-time regulation, and is right again the preferential real-time regulation of opening aperture, inclination and the water injection temperature of water filling port is right at last agitating unit's stirring vane quantity, stirring vane stretch out radius and stirring vane's rotational speed carries out real-time regulation.
Furthermore, the preset adjusting mode of each deviation value in the controller adopts a sequential interval adjusting mode.
Furthermore, the preset adjusting mode of each deviation value in the controller adopts a sequential overlapping adjusting mode.
Further, the preset adjusting mode of each deviation value in the controller can be adjusted by a user.
Furthermore, the controller records the corresponding change of each adjustment parameter and the detection data of the sampling detection port after adjustment, and periodically optimizes the sludge concentration coefficient, the sludge particle size coefficient and the sludge flow coefficient in the priority adjustment unit after multiple adjustments are aggregated.
Further, the invention also provides a simple sludge slurrying method, which is characterized by comprising the following steps: the method comprises the following steps:
1) continuously introducing sludge into the raw material pump;
2) waste heat hot water and sludge are introduced into the raw material pump through a water injection port formed at a feed inlet above the raw material pump to realize mixing;
3) starting a power source, wherein an output shaft of the power source drives a stirring device in the raw material pump through a transmission to stir the sludge in the raw material pump;
4) the stirred sludge sequentially passes through the pipeline and the elbow, and secondary stirring and mixing are realized by utilizing the collision between the sludge and the sludge resistance area on the inner wall of the pipeline and the elbow;
5) the sludge changes the flowing direction in the pipeline through the turbulator to realize further and sufficient mixing of the sludge and the hot water;
6) the sampling detection port arranged on the turbulator is used for detecting the parameters of the sludge after mixing and stirring, and the controller realizes corresponding adjustment according to the detection data of the sampling detection port and the adjustment requirement, the adjustment mode and the adjustment priority determined in the priority adjustment unit;
7) and recording the corresponding change of each adjusting parameter and the detecting data of the sampling detecting port after adjustment in the controller, and periodically optimizing the sludge concentration coefficient, the sludge particle size coefficient and the sludge flow coefficient in the priority adjusting unit after multiple times of adjustment and convergence.
The invention has the advantages that;
(1) according to the technical scheme provided by the invention, mechanical equipment such as a spiral slurrying machine, a slurrying machine water tank, a slurrying machine middle storage bin, a sludge conveying pump and the like in the original scheme are omitted, the operation is more convenient and more operable, the equipment investment cost of project construction is greatly saved, and meanwhile, the concentration, the particle size and the flow parameter of the mixed sludge detected by a sampling detection port realize parameter adjustment on the position of a water injection port, adjustment on the corresponding parameter of a stirring device and corresponding adjustment on the corresponding parameter of a pipeline and an elbow according to the adjustment requirement, the adjustment mode and the adjustment priority determined in a priority adjustment unit, so that the efficiency and the accuracy of sludge mixing and slurrying are effectively improved, and meanwhile, the further improvement of a slurrying system and a slurrying method are further realized through continuous optimization.
Drawings
FIG. 1 is a schematic structural diagram of the present invention.
Detailed Description
The present invention will now be described in further detail with reference to the accompanying drawings. These drawings are simplified schematic views illustrating only the basic structure of the present invention in a schematic manner, and thus show only the constitution related to the present invention.
The technical scheme provided by the invention is as follows:
the utility model provides a simple and easy sludge slurrying system, include and install feedstock pump 2 on base station 7 through support 8, water filling port 1-1 has been seted up on feedstock pump 2's top feed inlet 1, be provided with pipeline 9 and elbow 10 in one side of feedstock pump 2, the export of elbow 10 is connected with turbulator 3, opposite side at feedstock pump 2 is provided with power supply 5 and derailleur 6, the output shaft of power supply 5 is connected with the inside agitating unit of feedstock pump 2 through derailleur 6, the outside of power supply 5 still is connected with controller 4, its characterized in that:
the opening aperture, the inclination angle and the water injection temperature of the water injection port 1-1 can be adjusted in real time through the controller 4;
the number of the stirring blades of the stirring device, the extension radius of the stirring blades, and the rotating speed of the stirring blades can be adjusted in real time by the controller 4;
mud resistance areas extend out of the inner walls of the pipeline 9 and the elbow 10, and the number and the area of the mud resistance areas and the angle of the corner of the elbow 10 can be adjusted in real time through the controller 4;
the turbulator 3 is provided with a sampling detection port 3-1, the controller 4 is internally provided with a priority adjusting unit, and the controller 4 realizes corresponding adjustment according to the detection data of the sampling detection port 3-1 and according to the adjustment requirement, the adjustment mode and the adjustment priority determined in the priority adjusting unit.
Specifically, the detection data of the sampling detection port 3-1 at least comprises concentration detection data, particle size detection data and flow detection data, so that the speech effect of the sludge after mixing and stirring is obtained from the concentration data, the particle size data and the flow data of the sludge respectively.
Specifically, the preset regulation requirements in the priority regulation unit satisfy:
Y＝aY1+bY2+cY3 (1)
wherein the content of the first and second substances,
y represents a regulation demand value determined in the priority regulation unit;
y0 represents a regulation demand value preset in the priority regulation unit;
when Y is more than Y0, starting the controller to realize corresponding adjustment; when Y is less than Y0, the controller is not started to realize corresponding adjustment;
a represents a sludge concentration coefficient;
b represents a sludge particle size coefficient;
c represents a sludge flow coefficient;
y1 represents a deviation value of sludge concentration and satisfies
Y1＝|X1-X10|/X10 (2)
Wherein the content of the first and second substances,
x1 represents an actual measurement value of the sludge concentration,
x10 denotes a preset sludge concentration value;
y2 represents a deviation value of sludge particle size and satisfies
Y2＝|X2-X20|/X20 (3)
Wherein the content of the first and second substances,
x2 represents an actual measurement value of the sludge particle diameter,
x20 represents a preset value of sludge particle size;
y3 represents a deviation value of the sludge flow rate and satisfies
Y3＝|X3-X30|/X30 (4)
Wherein the content of the first and second substances,
x3 represents the measured value of the sludge flow rate,
x30 represents a preset sludge flow rate value;
specifically, the priority adjusting unit sequences the sludge concentration deviation value Y1, the sludge particle size deviation value Y2 and the sludge flow deviation value Y3 in sequence, and selects the preset adjusting mode corresponding to the maximum value as the adjusting mode of the current controller, so that the adjusting of the sludge slurrying process is realized in the most direct and intuitive adjusting mode according to the preset adjusting mode with the maximum deviation value as the adjusting mode of the current controller, and the accuracy and the adjusting efficiency of the sludge slurrying adjustment are improved.
Specifically, the preset regulation mode of the controller 4 for the sludge concentration deviation value Y1 is to preferentially regulate the opening aperture, the inclination angle and the water injection temperature of the water injection port 1-1 in real time, secondly, adjusting the number and the area of mud resistance areas extending out of the inner walls of the pipeline 9 and the elbow 10 and the corner radius of the elbow 10 in real time, finally adjusting the number of stirring blades of the stirring device, the extending radius of the stirring blades and the rotating speed of the stirring blades in real time, wherein the largest factor influencing the sludge concentration is the parameter of the added waste heat hot water, therefore, the aperture and the inclination angle of the opening of the water injection port 1-1 and the water injection temperature need to be preferentially adjusted in real time so as to preferentially adjust the parameters of the waste heat hot water, secondly, relevant parameters of the muddy water when the pipeline and the elbow are mixed and relevant parameters of the stirring device need to be controlled;
the preset adjusting mode of the controller 4 for the sludge particle size deviation value Y2 is to perform preferential real-time adjustment on the number of stirring blades of the stirring device, the extension radius of the stirring blades and the rotating speed of the stirring blades, then perform real-time adjustment on the number and area of mud resistance areas extending out of the inner walls of the pipeline 9 and the elbow 10 and the corner radius of the elbow 10, and finally perform preferential real-time adjustment on the opening aperture, the inclination angle and the water injection temperature of the water injection port 1-1; the largest factor influencing the sludge particle size is related parameters in the stirring process, so that the related parameters of the stirring device need to be preferentially adjusted, and then the parameters of waste heat hot water and the related parameters of muddy water when the pipeline and the elbow are mixed need to be controlled;
the preset adjusting mode of the controller 4 for the sludge flow deviation value Y3 is to perform preferential real-time adjustment on the number and area of sludge resistance areas extending out of the inner walls of the pipeline 9 and the elbow 10 and the corner radius of the elbow 10, to perform preferential real-time adjustment on the opening aperture, the inclination angle and the water injection temperature of the water injection port 1-1, and to perform real-time adjustment on the number of stirring blades of the stirring device, the extension radius of the stirring blades and the rotating speed of the stirring blades; the biggest factor influencing the flow of the sludge is related parameters during mixing of the muddy water, so that the related parameters of the muddy water during mixing of the pipeline and the elbow are required to be preferentially adjusted, and then the parameters of the waste heat hot water and the related parameters of the stirring device are required to be controlled.
Specifically, the preset adjustment mode for each deviation value in the controller 4 is an interval adjustment mode, so that the corresponding change of the detection parameter caused by the adjustment mode of each interval is compared during statistics, and further optimization and improvement of the slurrying system and method are facilitated.
Specifically, the preset adjustment mode for each deviation value in the controller 4 is a sequential overlapping adjustment mode, so as to facilitate stable transition and handover of the slurrying system and method during adjustment.
Specifically, the preset adjusting mode for each deviation value in the controller 4 can be adjusted by the user, so that the user can conveniently adjust the deviation values according to the own requirements.
Specifically, the controller 4 records the adjustment parameters each time and the corresponding changes of the detection data of the sampling detection port 3-1 after adjustment, and periodically optimizes the sludge concentration coefficient, the sludge particle size coefficient and the sludge flow coefficient in the priority adjustment unit after multiple times of adjustment and convergence.
Specifically, the invention also provides a simple sludge slurrying method, which is characterized by comprising the following steps: the method comprises the following steps:
1) continuously introducing sludge into the raw material pump;
2) waste heat hot water and sludge are introduced into the raw material pump through a water injection port formed at a feed inlet above the raw material pump to realize mixing;
3) starting a power source, wherein an output shaft of the power source drives a stirring device in the raw material pump through a transmission to stir the sludge in the raw material pump;
4) the stirred sludge sequentially passes through the pipeline and the elbow, and secondary stirring and mixing are realized by utilizing the collision between the sludge and the sludge resistance area on the inner wall of the pipeline and the elbow;
5) the sludge changes the flowing direction in the pipeline through the turbulator to realize further and sufficient mixing of the sludge and the hot water;
6) the sampling detection port arranged on the turbulator is used for detecting the parameters of the sludge after mixing and stirring, and the controller realizes corresponding adjustment according to the detection data of the sampling detection port and the adjustment requirement, the adjustment mode and the adjustment priority determined in the priority adjustment unit;
7) and recording the corresponding change of each adjusting parameter and the detecting data of the sampling detecting port after adjustment in the controller, and periodically optimizing the sludge concentration coefficient, the sludge particle size coefficient and the sludge flow coefficient in the priority adjusting unit after multiple times of adjustment and convergence.
In light of the foregoing description of the preferred embodiment of the present invention, many modifications and variations will be apparent to those skilled in the art without departing from the spirit and scope of the invention. The technical scope of the present invention is not limited to the content of the specification, and must be determined according to the scope of the claims.
Claims (10)
1. The utility model provides a simple and easy sludge slurrying system, include and install former pump (2) on base station (7) through support (8), water filling port (1-1) have been seted up on top feed inlet (1) of former pump (2), be provided with pipeline (9) and elbow (10) in one side of former pump (2), the export and the turbulator (3) of elbow (10) are connected, opposite side at former pump (2) is provided with power supply (5) and derailleur (6), the output shaft of power supply (5) is connected with the inside agitating unit of former pump (2) through derailleur (6), the outside of power supply (5) still is connected with controller (4), its characterized in that:
the opening aperture, the inclination angle and the water injection temperature of the water injection port (1-1) can be adjusted in real time through the controller (4);
the number of the stirring blades of the stirring device, the extending radius of the stirring blades and the rotating speed of the stirring blades can be adjusted in real time through the controller (4);
mud resistance areas extend out of the inner walls of the pipeline (9) and the elbow (10), and the number and the area of the mud resistance areas and the corner angle of the elbow (10) can be adjusted in real time through the controller (4);
the turbulator (3) is provided with a sampling detection port (3-1), a priority adjusting unit is arranged in the controller (4), and the controller (4) realizes corresponding adjustment according to the detection data of the sampling detection port (3-1) and according to the adjustment requirement, the adjustment mode and the adjustment priority determined in the priority adjusting unit.
2. The simple sludge slurrying system of claim 1 wherein: the detection data of the sampling detection port (3-1) at least comprises concentration detection data, particle size detection data and flow detection data.
3. The simple sludge slurrying system of claim 2 wherein: the preset regulation requirements in the priority regulation unit meet:
Y＝aY1+bY2+cY3 (1)
wherein the content of the first and second substances,
y represents a regulation demand value determined in the priority regulation unit;
y0 represents a regulation demand value preset in the priority regulation unit;
when Y is more than Y0, starting the controller to realize corresponding adjustment; when Y is less than Y0, the controller is not started to realize corresponding adjustment;
a represents a sludge concentration coefficient;
b represents a sludge particle size coefficient;
c represents a sludge flow coefficient;
y1 represents a deviation value of sludge concentration and satisfies
Y1＝|X1-X10|/X10 (2)
Wherein the content of the first and second substances,
x1 represents an actual measurement value of the sludge concentration,
x10 denotes a preset sludge concentration value;
y2 represents a deviation value of sludge particle size and satisfies
Y2＝|X2-X20|/X20 (3)
Wherein the content of the first and second substances,
x2 represents an actual measurement value of the sludge particle diameter,
x20 represents a preset value of sludge particle size;
y3 represents a deviation value of the sludge flow rate and satisfies
Y3＝|X3-X30|/X30 (4)
Wherein the content of the first and second substances,
x3 represents the measured value of the sludge flow rate,
x30 denotes the preset sludge flow value.
4. The simple sludge slurrying system of claim 3 wherein: the priority adjusting unit is used for sequencing the sludge concentration deviation value Y1, the sludge particle size deviation value Y2 and the sludge flow deviation value Y3 in sequence, and selecting a preset adjusting mode corresponding to the maximum value as the adjusting mode of the current controller.
5. The simple sludge slurrying system of claim 4 wherein: the preset adjusting mode of the controller (4) for the sludge concentration deviation value Y1 is to preferentially adjust the opening aperture, the inclination angle and the water injection temperature of the water injection port (1-1) in real time, then adjust the number and the area of the sludge resistance areas extending out of the inner walls of the pipeline (9) and the elbow (10) and the corner radius of the elbow (10) in real time, and finally adjust the number of stirring blades of the stirring device, the extending radius of the stirring blades and the rotating speed of the stirring blades in real time;
the preset adjusting mode of the controller (4) for the sludge particle size deviation value Y2 is to perform preferential real-time adjustment on the number of stirring blades of the stirring device, the extension radius of the stirring blades and the rotating speed of the stirring blades, then perform real-time adjustment on the number and the area of mud resistance areas extending out of the inner walls of the pipeline (9) and the elbow (10) and the corner radius of the elbow (10), and finally perform preferential real-time adjustment on the opening aperture, the inclination angle and the water injection temperature of the water injection port (1-1);
the regulation mode that predetermines mud flow deviation value Y3 in controller (4) is right the mud that the inner wall of pipeline (9) and elbow (10) stretches out the setting hinders regional quantity, area and elbow (10) the corner radius carries out preferential real-time regulation, and is right again the preferential real-time regulation of opening aperture, inclination and the water injection temperature of water filling port (1-1), it is right again at last agitating unit's stirring vane quantity, stirring vane stretch out radius and stirring vane's rotational speed carries out real-time regulation.
6. The simple sludge slurrying system of claim 5 wherein: and the controller (4) adopts a sequential interval regulation mode for regulating the preset deviation values.
7. The simple sludge slurrying system of claim 5 wherein: and the controller (4) adopts a sequential overlapping adjustment mode for the preset adjustment modes of the deviation values.
8. The simple sludge slurrying system of claim 5 wherein: the preset adjusting mode of each deviation value in the controller (4) can be adjusted by a user.
9. The simple sludge slurrying system of claim 3 wherein: and the controller (4) records the adjustment parameters of each time and the corresponding change of the detection data of the sampling detection port (3-1) after adjustment, and periodically optimizes the sludge concentration coefficient, the sludge particle size coefficient and the sludge flow coefficient in the priority adjustment unit after multiple times of adjustment and convergence.
10. A simple sludge slurrying method is characterized by comprising the following steps: the method comprises the following steps:
1) continuously introducing sludge into the raw material pump;
2) waste heat hot water and sludge are introduced into the raw material pump through a water injection port formed at a feed inlet above the raw material pump to realize mixing;
3) starting a power source, wherein an output shaft of the power source drives a stirring device in the raw material pump through a transmission to stir the sludge in the raw material pump;
4) the stirred sludge sequentially passes through the pipeline and the elbow, and secondary stirring and mixing are realized by utilizing the collision between the sludge and the sludge resistance area on the inner wall of the pipeline and the elbow;
5) the sludge changes the flowing direction in the pipeline through the turbulator to realize further and sufficient mixing of the sludge and the hot water;
6) the sampling detection port arranged on the turbulator is used for detecting the parameters of the sludge after mixing and stirring, and the controller realizes corresponding adjustment according to the detection data of the sampling detection port and the adjustment requirement, the adjustment mode and the adjustment priority determined in the priority adjustment unit;
7) and recording the corresponding change of each adjusting parameter and the detecting data of the sampling detecting port after adjustment in the controller, and periodically optimizing the sludge concentration coefficient, the sludge particle size coefficient and the sludge flow coefficient in the priority adjusting unit after multiple times of adjustment and convergence.
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| CN112807731A (en) * | 2020-12-29 | 2021-05-18 | 广西桂平悦达香料有限公司 | Production and preparation process and device of cinnamon hydrolat |
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