CN111796615A

CN111796615A - Thermal balance control method and related equipment

Info

Publication number: CN111796615A
Application number: CN201910282013.5A
Authority: CN
Inventors: 莫乙玟; 黄晓丽; 蒋晓明; 吕胜军
Original assignee: Shenzhen Jiajia Classification Technology Co ltd
Current assignee: Shenzhen Jiajia Classification Technology Co ltd
Priority date: 2019-04-09
Filing date: 2019-04-09
Publication date: 2020-10-20
Anticipated expiration: 2039-04-09
Also published as: CN111796615B

Abstract

The embodiment of the application discloses a heat balance control method and related equipment, wherein the method comprises the following steps: acquiring the current temperature in a cabin of the biochemical degradation equipment; if the current temperature is greater than or equal to the set critical temperature, determining the temperature difference between the current temperature and the set critical temperature; determining at least one temperature control module based on the temperature difference; and adjusting the temperature in the biochemical degradation equipment cabin by adopting a preset temperature control method based on at least one temperature control module so as to obtain that the temperature in the biochemical degradation equipment cabin is in a set temperature range. By adopting the embodiment of the application, when the biochemical degradation equipment is in a working state, the temperature in the biochemical degradation equipment cabin is in a set temperature range, and the garbage degradation efficiency is favorably improved.

Description

Thermal balance control method and related equipment

Technical Field

The application relates to the technical field of temperature control, in particular to a heat balance control method and related equipment.

Background

When the biochemical degradation equipment is in a working state, the temperature in the biochemical degradation equipment chamber needs to be in a certain temperature range. At present, when the temperature in a biochemical degradation equipment cabin is low, the biochemical degradation equipment controls a heating rod to start heating heat conduction oil so as to raise the temperature in the cabin; when the temperature in the biochemical degradation equipment cabin is higher, the biochemical degradation equipment controls the heating rod to stop heating the heat conduction oil so as to reduce the temperature in the cabin. Because the biochemical degradation equipment degrades the rubbish for a long time, the temperature in the biochemical degradation equipment cabin can not be stabilized within a certain temperature range for a long time due to the repeated heating mode, and then the rubbish degradation efficiency is influenced.

Disclosure of Invention

The embodiment of the application provides a heat balance control method and related equipment, which are used for enabling the temperature in a biochemical degradation equipment cabin to be in a set temperature range when the biochemical degradation equipment is in a working state, and are beneficial to improving the garbage degradation efficiency.

The first aspect of the embodiment of the application provides a thermal balance control method, is applied to biochemical degradation equipment, biochemical degradation equipment include the cabin body, set up in the cabin cover of cabin body upside, set up in garbage bin traction system and the condensation port of cabin body side, set up in the vapor drainage system and the condensation system of condensation port, set up in the degradation groove of internal portion of cabin, set up in the regional mixing system of degradation groove and degradation agent throw the material device, set up in the regional conduction oil heating system of degradation groove and set up in the hot air device of the cabin body, be equipped with in the degradation groove through garbage bin traction system with the waiting to degrade rubbish that the pan feeding mouth of cabin cover emptys, the method includes:

acquiring the current temperature in the biochemical degradation equipment cabin;

if the current temperature is greater than or equal to a set critical temperature, determining a temperature difference value between the current temperature and the set critical temperature;

determining at least one temperature control module based on the temperature difference;

and adjusting the temperature in the biochemical degradation equipment cabin by adopting a preset temperature control method based on the at least one temperature control module so as to obtain that the temperature in the biochemical degradation equipment cabin is in a set temperature range.

The second aspect of the embodiment of the application provides a biochemical degradation equipment, biochemical degradation equipment include the cabin body, set up in the cabin cover of cabin body upside, set up in garbage bin traction system and the condensation port of cabin body side, set up in the vapor drainage system and the condensation system of condensation port, set up in the inside degradation groove of cabin body, set up in the regional mixing system of degradation groove and degradation agent throw the material device, set up in the regional conduction oil heating system of degradation groove with set up in the hot air device of the cabin body, be equipped with in the degradation groove and pass through garbage bin traction system with what the pan feeding mouth of cabin cover was emptyd treats degradation rubbish, equipment includes:

the first acquisition unit is used for acquiring the current temperature in the biochemical degradation equipment cabin;

the first determining unit is used for determining the temperature difference between the current temperature and the set critical temperature if the current temperature is greater than or equal to the set critical temperature;

a second determination unit for determining at least one temperature control module based on the temperature difference value;

and the adjusting unit is used for adjusting the temperature in the biochemical degradation equipment cabin by adopting a preset temperature control method based on the at least one temperature control module so as to obtain that the temperature in the biochemical degradation equipment cabin is in a set temperature range.

A third aspect of embodiments of the present application provides a biochemical degradation apparatus comprising a processor, a memory, a communication interface, and one or more programs, the one or more programs being stored in the memory and configured to be executed by the processor, the programs comprising instructions for performing some or all of the steps of the method of the first aspect of embodiments of the present application.

A fourth aspect of embodiments of the present application provides a computer-readable storage medium for storing a computer program for electronic data exchange, the computer program enabling a computer to perform some or all of the steps described in the method according to the first aspect of embodiments of the present application.

A fifth aspect of embodiments of the present application provides a computer program product comprising a non-transitory computer readable storage medium storing a computer program operable to cause a computer to perform some or all of the steps described in the method according to the first aspect of embodiments of the present application. The computer program product may be a software installation package.

It can be seen that, in the embodiment of the present application, when the current temperature in the biochemical degradation equipment chamber is greater than or equal to the set critical temperature, the biochemical degradation equipment determines at least one temperature control module based on a temperature difference between the current temperature and the set critical temperature, and adjusts the temperature in the biochemical degradation equipment chamber by using a preset temperature control method based on the at least one temperature control module. Compared with the biochemical degradation equipment, the heating rod is controlled to repeatedly heat the heat conduction oil, so that the temperature in the biochemical degradation equipment cabin cannot be stabilized within a certain temperature range for a long time, the temperature in the biochemical degradation equipment cabin is adjusted by adopting a preset temperature control method based on at least one temperature control module, and therefore when the biochemical degradation equipment is in a working state, the temperature in the biochemical degradation equipment cabin is within a set temperature range, and the garbage degradation efficiency is improved.

Drawings

In order to more clearly illustrate the technical solutions in the embodiments or the background art of the present application, the drawings required to be used in the embodiments or the background art of the present application will be described below.

FIG. 1 is a schematic structural diagram of a biochemical degradation apparatus provided in an embodiment of the present application;

FIG. 2 is a schematic flow chart illustrating a method for controlling thermal balance according to an embodiment of the present disclosure;

FIG. 3 is a schematic flow chart diagram illustrating another method for controlling thermal balance according to an embodiment of the present disclosure;

FIG. 4 is a block diagram of functional units of a biochemical degradation apparatus according to an embodiment of the present disclosure;

fig. 5 is a schematic structural diagram of another biochemical degradation apparatus provided in an embodiment of the present application.

Detailed Description

The technical solutions in the embodiments of the present application will be clearly and completely described below with reference to the drawings in the embodiments of the present application, and it is obvious that the described embodiments are only a part of the embodiments of the present application, and not all of the embodiments. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present application.

The terms "first," "second," and the like in the description and claims of the present application and in the above-described drawings are used for distinguishing between different objects and not for describing a particular order. Furthermore, the terms "include" and "have," as well as any variations thereof, are intended to cover non-exclusive inclusions. For example, a process, method, system, article, or apparatus that comprises a list of steps or elements is not limited to only those steps or elements listed, but may alternatively include other steps or elements not listed, or inherent to such process, method, article, or apparatus.

Reference in the specification to "an embodiment" means that a particular feature, structure, or characteristic described in connection with the embodiment can be included in at least one embodiment of the specification. The appearances of the phrase in various places in the specification are not necessarily all referring to the same embodiment, nor are separate or alternative embodiments mutually exclusive of other embodiments. It is explicitly and implicitly understood by one skilled in the art that the embodiments described herein can be combined with other embodiments.

Referring to fig. 1, fig. 1 is a schematic structural diagram of a biochemical degradation apparatus provided in an embodiment of the present application, where the biochemical degradation apparatus 100 includes a cabin 101, a cabin cover 102 disposed on an upper side of the cabin 101, a garbage can traction system 103 and a condensation port 104 disposed on a side of the cabin 101, a water vapor drainage system 105 and a condensation system 106 disposed on the condensation port 104, a degradation tank 107 disposed inside the cabin 101, a stirring system 108 and a degrading agent feeding device 109 disposed in a region of the degradation tank 107, a heat-conducting oil heating system 110 disposed in a region of the degradation tank 107, a hot air device 111 disposed on the cabin 101, a temperature sensor 112 disposed in a region of the degradation tank 107, and a processor 113 disposed on a side of the cabin 101, where to-be-degraded garbage is dumped through a material inlet of the garbage can traction system 103 and the cabin cover 102 in the degradation tank 107, where:

a temperature sensor 112, configured to obtain a current temperature in the biochemical degradation equipment compartment;

a processor 113, configured to determine a temperature difference between the current temperature and a set threshold temperature if the current temperature is greater than or equal to the set threshold temperature; determining at least one temperature control module based on the temperature difference; and adjusting the temperature in the biochemical degradation equipment cabin by adopting a preset temperature control method based on the at least one temperature control module so as to obtain that the temperature in the biochemical degradation equipment cabin is in a set temperature range.

Referring to fig. 2, fig. 2 is a schematic flow chart of a thermal balance control method according to an embodiment of the present application, the thermal balance control method is applied to the biochemical degradation apparatus shown in fig. 1, and the thermal balance control method includes

steps

201 and 204 as follows:

201: and the biochemical degradation equipment acquires the current temperature in the biochemical degradation equipment cabin.

The biochemical degradation device may be a device for instantly degrading the garbage to be degraded, and is not limited herein.

Wherein, the current temperature in the cabin of the biochemical degradation equipment is measured by a temperature sensor of the biochemical degradation equipment.

The current temperature is the sum of the temperature generated by the heat-conducting oil heating system, the temperature generated by the hot air device, the temperature generated by the stirring system, the temperature reduced by the water vapor drainage system and the condensation system and the temperature generated by the degrading agent feeding device.

202: and if the current temperature is greater than or equal to the set critical temperature, the biochemical degradation equipment determines the temperature difference between the current temperature and the set critical temperature.

The set critical temperature can be self-defined by a user or a biochemical degradation device, and is less than 100 ℃.

203: the biochemical degradation device determines at least one temperature control module based on the temperature difference.

The temperature control module comprises a heat conduction oil control module, a hot air control module, a garbage stirring control module, a steam condensation control module and a degradation agent control module, the heat conduction oil control module comprises a heat conduction oil heating system, the hot air control module comprises a hot air device, the garbage stirring control module comprises a stirring system, the steam condensation control module comprises a steam drainage system and a condensation system, and the degradation agent control module comprises a degradation agent feeding device.

In one possible example, the biochemical degradation apparatus determines at least one temperature control module based on the temperature difference, including:

if the temperature difference is smaller than the first temperature, the biochemical degradation equipment determines that the at least one temperature control module comprises a garbage stirring control module and a degradation agent control module;

if the temperature difference is greater than or equal to the first temperature and less than the second temperature, the biochemical degradation equipment determines that the at least one temperature control module comprises a hot air control module, a water vapor condensation control module and a degradation agent control module;

if the temperature difference is greater than or equal to the second temperature and less than a third temperature, the biochemical degradation equipment determines that the at least one temperature control module comprises a hot air control module, a garbage stirring control module, a water vapor condensation control module and a degradation agent control module;

if the temperature difference is greater than or equal to a fourth temperature and less than a fifth temperature, the biochemical degradation equipment determines that the at least one temperature control module comprises a heat conduction oil control module, a garbage stirring control module and a degradation agent control module;

if the temperature difference is greater than or equal to a fifth temperature and less than a sixth temperature, the biochemical degradation equipment determines that the at least one temperature control module comprises a heat conduction oil control module, a hot air control module, a water vapor condensation control module and a degradation agent control module;

and if the temperature difference is greater than or equal to the sixth temperature, the biochemical degradation equipment determines that the at least one temperature control module comprises a heat conduction oil control module, a hot air control module, a garbage stirring control module, a steam condensation control module and a degradation agent control module.

204: and the biochemical degradation equipment adjusts the temperature in the biochemical degradation equipment cabin by adopting a preset temperature control method based on the at least one temperature control module so as to obtain that the temperature in the biochemical degradation equipment cabin is in a set temperature range.

The set temperature range comprises a set lowest temperature and a set highest temperature, the set lowest temperature and the set highest temperature can be defined by a user or biochemical degradation equipment, the set critical temperature is greater than the set lowest temperature and less than the set highest temperature, and the set highest temperature is less than 100 ℃.

In one possible example, the at least one temperature control module includes a heat conduction oil control module and a degradation agent control module, and the biochemical degradation device adjusts the temperature in the biochemical degradation device chamber based on the at least one temperature control module by adopting a preset temperature control method, including:

the biochemical degradation equipment determines a first heat corresponding to the temperature difference value based on a pre-stored heat-temperature calculation formula;

the biochemical degradation equipment acquires a first temperature change rate in the biochemical degradation equipment cabin, and determines first temperature change duration based on the first temperature change rate and the temperature difference;

the biochemical degradation equipment acquires the weight of a first degradation agent corresponding to the degradation agent control module and the current working power of the heat conduction oil control module, and determines a second heat corresponding to the degradation agent control module based on the weight of the first degradation agent, the temperature difference, the first temperature change time length and a prestored degradation agent heat calculation formula;

the biochemical degradation equipment determines a first heat difference value between the first heat and the second heat, and determines a first working power adjusted by the heat conduction oil control module based on the first heat difference value, the current working power of the heat conduction oil control module, the first temperature change time length and a pre-stored heat conduction oil calculation formula;

and the biochemical degradation equipment adjusts the working power of the heat conduction oil control module to be the first working power.

Wherein the heat-temperature calculation formula is:

Q₁＝C₁×M×F₁，

Q₁is the first heat quantity, C, corresponding to the temperature difference₁Is the mass of the waste to be degraded, M is the specific heat capacity of the waste to be degraded, F₁The temperature difference is obtained, the mass of the garbage to be degraded is measured by a gravity sensor of the biochemical degradation equipment, and the specific heat capacity of the garbage to be degraded can be self-defined by a user or calculated by the biochemical degradation equipment.

Specifically, the embodiment of the biochemical degradation device acquiring the first temperature change rate in the cabin of the biochemical degradation device may be: the method comprises the following steps that the biochemical degradation equipment obtains N temperatures in a cabin of the biochemical degradation equipment, wherein N is an integer larger than 1; the biochemical degradation equipment groups the N temperatures to obtain M groups of temperature sets, wherein each group of temperature sets comprises N/M temperatures, and M is an integer greater than or equal to 1; the biochemical degradation equipment respectively determines the temperature change rate of each group of temperature sets to obtain M temperature change rates; the biochemical degradation device determines a first temperature change rate based on the M temperature change rates and a pre-stored temperature change rate prediction algorithm.

Wherein the first temperature change duration is a ratio of the temperature difference to the first temperature change rate.

The biochemical degradation equipment obtains the weight of a first degradation agent corresponding to the degradation agent control module through the degradation agent feeding device.

Wherein, the heat calculation formula of the degradation agent is as follows:

Q₂＝C₂×F₁×T₁×α，

Q₂is the second heat corresponding to the degradation agent control module, C₂Is the weight of the first degradation agent, F₁Is the temperature difference, T₁Is the first temperature change duration, α is the thermal constant of the degradation agent in units of: degrees celsius/(mass x temperature x time).

Wherein, the heat quantity calculation formula of the heat transfer oil is as follows:

P₁＝P₂-Q₃/T₁，

Q₃is the first heat difference, P₁Is the first working power, P, regulated by the heat-conducting oil control module₂Is the current operating power, T, of the heat transfer oil control module₁Is a first temperature change duration.

In one possible example, the at least one temperature control module comprises a hot air control module, a water vapor condensation control module and a degradation agent control module, and the biochemical degradation device adjusts the temperature in the biochemical degradation device chamber based on the at least one temperature control module by adopting a preset temperature control method, and the method comprises the following steps:

the biochemical degradation equipment determines a third heat corresponding to the temperature difference value based on the heat-temperature calculation formula;

the biochemical degradation equipment acquires a second temperature change rate in the biochemical degradation equipment cabin, and determines a second temperature change duration based on the second temperature change rate and the temperature difference;

the biochemical degradation equipment acquires the weight of a second degradation agent corresponding to the degradation agent control module and the current working power of the hot air control module, and determines a fourth heat corresponding to the degradation agent control module based on the weight of the second degradation agent, the temperature difference value, the second temperature change time length and the degradation agent heat calculation formula;

the biochemical degradation equipment determines a second heat difference value of the third heat and the fourth heat, and obtains a second working power adjusted by the hot air control module based on the second heat difference value, the current working power of the hot air control module, the second temperature change time length and a pre-stored hot air-steam heat calculation formula;

and the biochemical degradation equipment adjusts the working power of the hot air control module to be the second working power.

Wherein, the hot air-water vapor heat quantity calculation formula is as follows:

P₃＝P₄-Q₄/(T₂-H×L×T₂×β)，

Q₄is the second heat difference, P₄Is the current work of the hot air control moduleRate, P₃Is the second working power, T, adjusted by the hot air control module₂The second temperature change duration is, H is rated torque, L is the size of a condensation port, beta is the heat corresponding to the water vapor in unit volume, and H, L and beta can be defined by a user or biochemical degradation equipment.

It can be seen that, in this example, since the energy consumption is greater to some extent when the temperature inside the biochemical degradation apparatus is adjusted using the conduction oil control module and the degradation agent control module than when the temperature inside the biochemical degradation apparatus is adjusted using the hot air control module, the water vapor condensation control module, and the degradation agent control module, the energy consumption of the biochemical degradation apparatus is reduced.

In one possible example, the at least one temperature control module includes a garbage stirring control module and a degrading agent control module, and the biochemical degradation device adjusts the temperature in the biochemical degradation device chamber based on the at least one temperature control module by adopting a preset temperature control method, including:

the biochemical degradation equipment determines a fifth heat corresponding to the temperature difference value based on the heat-temperature calculation formula;

the biochemical degradation equipment acquires a third temperature change rate in the biochemical degradation equipment cabin, and determines a third temperature change duration based on the third temperature change rate and the temperature difference;

the biochemical degradation equipment acquires a third degradation agent weight corresponding to the degradation agent control module and the current working power of the garbage stirring control module, and determines a sixth heat corresponding to the degradation agent control module based on the third degradation agent weight, the temperature difference, the third temperature change time length and the degradation agent heat calculation formula;

the biochemical degradation equipment determines a third heat difference value of the fifth heat and the sixth heat, and determines a third working power adjusted by the garbage stirring control module based on the third heat difference value, the current working power of the garbage stirring control module, the third temperature change time length and a prestored stirring heat calculation formula;

and the biochemical degradation equipment adjusts the working power of the garbage stirring control module to be the third working power.

Wherein, the calculation formula of the stirring heat quantity is as follows:

Q₅＝(P₆-P₅)×T₃，

Q₅is the third heat difference, P₆Is the current working power, P, of the refuse mixing control module₅Is the third working power, T, after the garbage stirring control module adjusts₃Is a third temperature change period.

It can be seen that, in this example, since the energy consumption is greater when the temperature inside the biochemical degradation apparatus is adjusted using the conduction oil control module and the degradation agent control module to some extent than when the temperature inside the biochemical degradation apparatus is adjusted using the garbage stirring control module and the degradation agent control module, the energy consumption of the biochemical degradation apparatus is reduced.

In one possible example, the at least one temperature control module includes a heat conduction oil control module, a hot air control module, a water vapor condensation control module and a degradation agent control module, and the biochemical degradation device adjusts the temperature in the biochemical degradation device chamber based on the at least one temperature control module by adopting a preset temperature control method, including:

the biochemical degradation equipment determines a seventh heat corresponding to the temperature difference value based on the heat-temperature calculation formula;

the biochemical degradation equipment acquires a fourth temperature change rate in the biochemical degradation equipment cabin, and determines a fourth temperature change duration based on the fourth temperature change rate and the temperature difference;

the biochemical degradation equipment acquires a fourth degradation agent weight corresponding to the degradation agent control module, the current working power of the heat conduction oil control module and the current working power of the hot air control module, and determines an eighth heat corresponding to the degradation agent control module based on the fourth degradation agent weight, the temperature difference value, the fourth temperature change time length and the degradation agent heat calculation formula;

the biochemical degradation equipment determines a fourth heat difference value of the seventh heat and the eighth heat, and determines a ninth heat corresponding to the heat-conducting oil control module based on the fourth heat difference value and a first proportion corresponding to the heat-conducting oil control module;

the biochemical degradation equipment determines fourth working power adjusted by the heat conduction oil control module based on the ninth heat, the current working power of the heat conduction oil control module and the fourth temperature change duration;

the biochemical degradation equipment determines a fifth heat difference value of the fourth heat difference value and the ninth heat, and obtains a fifth working power adjusted by the hot air control module based on the fifth heat difference value, the current working power of the hot air control module, the fourth temperature change time length and the hot air-steam heat calculation formula;

and the biochemical degradation equipment adjusts the working power of the heat conduction oil control module to be the fourth working power, and adjusts the working power of the hot air control module to be the fifth working power.

The ninth heat corresponding to the heat conduction oil control module is the product of the fourth heat difference and a first proportion corresponding to the heat conduction oil control module, and the first proportion can be user-defined and can also be user-defined by biochemical degradation equipment.

It can be seen that, in this example, since the energy consumption is greater to adjust the temperature inside the biochemical degradation apparatus using the conduction oil control module and the degradation agent control module to some extent than to adjust the temperature inside the biochemical degradation apparatus using the conduction oil control module, the hot air control module, the steam condensation control module, and the degradation agent control module, the energy consumption of the biochemical degradation apparatus is reduced.

In one possible example, the at least one temperature control module comprises a heat conduction oil control module, a garbage stirring control module and a degradation agent control module, and the biochemical degradation equipment adjusts the temperature in the biochemical degradation equipment chamber based on the at least one temperature control module by adopting a preset temperature control method, and the method comprises the following steps:

the biochemical degradation equipment determines a tenth heat corresponding to the temperature difference value based on the heat-temperature calculation formula;

the biochemical degradation equipment acquires a fifth temperature change rate in the biochemical degradation equipment cabin, and determines a fifth temperature change duration based on the fifth temperature change rate and the temperature difference;

the biochemical degradation equipment acquires the weight of a fifth degradation agent corresponding to the degradation agent control module, the current working power of the heat conduction oil control module and the current working power of the garbage stirring control module, and determines the eleventh heat corresponding to the degradation agent control module based on the weight of the fifth degradation agent, the temperature difference, the fifth temperature change time and the degradation agent heat calculation formula;

the biochemical degradation equipment determines a sixth heat difference value of the tenth heat and the eleventh heat, and determines a twelfth heat corresponding to the heat-conducting oil control module based on the sixth heat difference value and a second proportion corresponding to the heat-conducting oil control module;

the biochemical degradation equipment determines the adjusted sixth working power of the heat conduction oil control module based on the twelfth heat, the current working power of the heat conduction oil control module and the fifth temperature change duration;

the biochemical degradation device determines a seventh heat difference value of the sixth heat and the twelfth heat, and determines a seventh working power adjusted by the garbage stirring control module based on the seventh heat difference value, the current working power of the garbage stirring control module, the fifth temperature change time length and the stirring heat calculation formula;

and the biochemical degradation equipment adjusts the working power of the heat conduction oil control module to be the sixth working power, and adjusts the working power of the garbage stirring control module to be the seventh working power.

It can be seen that, in this example, since the energy consumption is greater when the temperature inside the biochemical degradation apparatus is adjusted using the conduction oil control module and the degradation agent control module to some extent than when the temperature inside the biochemical degradation apparatus is adjusted using the conduction oil control module, the garbage stirring control module and the degradation agent control module, the energy consumption of the biochemical degradation apparatus can be reduced.

In one possible example, the at least one temperature control module includes a hot air control module, a garbage stirring control module, a water vapor condensation control module, and a degradation agent control module, and the biochemical degradation device adjusts the temperature in the biochemical degradation device cabin based on the at least one temperature control module by adopting a preset temperature control method, including:

the biochemical degradation device determines a thirteenth heat quantity corresponding to the temperature difference value based on the heat quantity-temperature calculation formula;

the biochemical degradation equipment acquires a sixth temperature change rate in the biochemical degradation equipment cabin, and determines a sixth temperature change duration based on the sixth temperature change rate and the temperature difference;

the biochemical degradation equipment acquires a sixth degradation agent weight corresponding to the degradation agent control module, the current working power of the hot air control module and the current working power of the garbage stirring control module, and determines a fourteenth heat quantity corresponding to the degradation agent control module based on the sixth degradation agent weight, the temperature difference value, the sixth temperature change time length and the degradation agent heat quantity calculation formula;

the biochemical degradation device determines an eighth heat difference value of the thirteenth heat and the fourteenth heat, and determines a fifteenth heat corresponding to the garbage stirring control module based on the eighth heat difference value and a third proportion corresponding to the garbage stirring control module;

the biochemical degradation device determines the eighth working power adjusted by the garbage stirring control module based on the fifteenth heat, the current working power of the garbage stirring control module and the sixth temperature change duration;

the biochemical degradation equipment determines a ninth heat difference value of the eighth heat difference value and the fifteenth heat, and obtains ninth working power adjusted by the hot air control module based on the ninth heat difference value, the current working power of the hot air control module, the sixth temperature change time length and the hot air-steam heat calculation formula;

and the biochemical degradation equipment adjusts the working power of the garbage stirring control module to be the eighth working power, and adjusts the working power of the hot air control module to be the ninth working power.

The fifteenth heat corresponding to the garbage stirring control module is the product of the eighth heat difference value and a third proportion corresponding to the garbage stirring control module, and the third proportion can be user-defined and can also be user-defined by biochemical degradation equipment.

It can be seen that, in this example, since the energy consumption is greater when the temperature inside the biochemical degradation apparatus is adjusted using the conduction oil control module and the degradation agent control module to some extent than when the temperature inside the biochemical degradation apparatus is adjusted using the hot air control module, the garbage stirring control module, the steam condensation control module, and the degradation agent control module, the energy consumption of the biochemical degradation apparatus is reduced.

In one possible example, the at least one temperature control module includes a heat conduction oil control module, a hot air control module, a garbage stirring control module, a water vapor condensation control module and a degradation agent control module, and the biochemical degradation device adjusts the temperature in the biochemical degradation device chamber based on the at least one temperature control module by adopting a preset temperature control method, including:

the biochemical degradation equipment determines a sixteenth heat corresponding to the temperature difference value based on the heat-temperature calculation formula;

the biochemical degradation equipment acquires a seventh temperature change rate in the biochemical degradation equipment cabin, and determines seventh temperature change duration based on the seventh temperature change rate and the temperature difference;

the biochemical degradation equipment acquires a seventh degradation agent weight corresponding to the degradation agent control module, the current working power of the heat conduction oil control module, the current working power of the hot air control module and the current working power of the garbage stirring control module, and determines a seventeenth heat corresponding to the degradation agent control module based on the seventh degradation agent weight, the temperature difference value, the seventh temperature change time length and the degradation agent heat calculation formula;

the biochemical degradation equipment determines a tenth heat difference value between the sixteenth heat and the seventeenth heat, and determines an eighteenth heat corresponding to the heat-conducting oil control module based on the tenth heat difference value and a fourth proportion corresponding to the heat-conducting oil control module;

the biochemical degradation equipment determines the tenth working power of the heat conduction oil control module after adjustment based on the eighteenth heat quantity, the current working power of the heat conduction oil control module and the seventh temperature change duration;

the biochemical degradation device determines an eleventh heat difference value of the tenth heat difference value and the eighteenth heat, and determines a nineteenth heat corresponding to the garbage stirring control module based on the eleventh heat difference value and a fifth proportion corresponding to the garbage stirring control module;

the biochemical degradation device determines eleventh working power adjusted by the garbage stirring control module based on the nineteenth heat, the current working power of the garbage stirring control module and the seventh temperature change duration;

the biochemical degradation equipment determines a twelfth heat difference value of the eleventh heat difference value and the nineteenth heat, and obtains twelfth working power adjusted by the hot air control module based on the twelfth heat difference value, the current working power of the hot air control module, the seventh temperature change time length and the hot air-steam heat calculation formula;

and the biochemical degradation equipment adjusts the working power of the heat conduction oil control module to be the tenth working power, adjusts the working evaluation rate of the garbage stirring control module to be the eleventh working power, and adjusts the working power of the hot air control module to be the twelfth working power.

It can be seen that, in this example, since the energy consumption is greater when the temperature inside the biochemical degradation apparatus is adjusted using the conduction oil control module and the degradation agent control module to some extent than when the temperature inside the biochemical degradation apparatus is adjusted using the conduction oil control module, the hot air control module, the garbage stirring control module, the water vapor condensation control module, and the degradation agent control module, the energy consumption of the biochemical degradation apparatus is reduced.

In one possible example, the method further comprises:

if the current temperature is greater than or equal to the set critical temperature, the biochemical degradation equipment acquires a target temperature change rate in the biochemical degradation equipment cabin;

the biochemical degradation device determines the at least one temperature control module based on the target temperature change rate;

and the biochemical degradation equipment adjusts the temperature in the biochemical degradation equipment cabin by adopting the preset temperature control method based on the at least one temperature control module so as to obtain that the temperature in the biochemical degradation equipment cabin is in the set temperature range.

The manner of acquiring the target temperature change rate in the biochemical degradation equipment chamber by the biochemical degradation equipment is the same as the manner of acquiring the first temperature change rate in the biochemical degradation equipment chamber, and the description is omitted here.

In one possible example, the biochemical degradation apparatus determines at least one temperature control module based on a target rate of temperature change, comprising:

if the target temperature change rate is smaller than a first threshold value, the biochemical degradation equipment determines that the at least one temperature control module comprises a garbage stirring control module and a degradation agent control module;

if the target temperature change rate is greater than or equal to a first threshold and less than a second threshold, the biochemical degradation equipment determines that the at least one temperature control module comprises a hot air control module, a water vapor condensation control module and a degradation agent control module;

if the target temperature change rate is greater than or equal to a second threshold and less than a third threshold, the biochemical degradation equipment determines that the at least one temperature control module comprises a hot air control module, a garbage stirring control module, a water vapor condensation control module and a degradation agent control module;

if the target temperature change rate is greater than or equal to a fourth threshold and less than a fifth threshold, the biochemical degradation equipment determines that the at least one temperature control module comprises a heat conduction oil control module, a garbage stirring control module and a degradation agent control module;

if the target temperature change rate is greater than or equal to a fifth threshold and less than a sixth threshold, the biochemical degradation equipment determines that the at least one temperature control module comprises a heat conduction oil control module, a hot air control module, a water vapor condensation control module and a degradation agent control module;

and if the target temperature change rate is greater than or equal to a sixth threshold value, the biochemical degradation equipment determines that the at least one temperature control module comprises a heat conduction oil control module, a hot air control module, a garbage stirring control module, a water vapor condensation control module and a degradation agent control module.

Referring to fig. 3, in accordance with the embodiment shown in fig. 2, fig. 3 is a schematic flow chart of another thermal balance control method provided in the embodiment of the present application, the thermal balance control method is applied to the biochemical degradation apparatus shown in fig. 1, and the thermal balance control method includes

steps

301 and 309, which are as follows:

301: and the biochemical degradation equipment acquires the current temperature in the biochemical degradation equipment cabin.

302: and if the current temperature is greater than or equal to the set critical temperature, the biochemical degradation equipment determines the temperature difference between the current temperature and the set critical temperature.

303: and the biochemical degradation equipment determines at least one temperature control module based on the temperature difference, and the at least one temperature control module comprises a heat conduction oil control module and a degradation agent control module.

304: and the biochemical degradation equipment determines a first heat corresponding to the temperature difference value based on a pre-stored heat-temperature calculation formula.

305: the biochemical degradation equipment obtains a first temperature change rate in the biochemical degradation equipment cabin, and determines a first temperature change duration based on the first temperature change rate and the temperature difference.

306: and the biochemical degradation equipment acquires the weight of a first degradation agent corresponding to the degradation agent control module and the current working power of the heat conduction oil control module, and determines the second heat corresponding to the degradation agent control module based on the weight of the first degradation agent, the temperature difference, the first temperature change time length and a prestored degradation agent heat calculation formula.

307: the biochemical degradation device determines a first heat difference between the first heat and the second heat.

308: and the biochemical degradation equipment determines the first working power adjusted by the heat conduction oil control module based on the first heat difference value, the current working power of the heat conduction oil control module, the first temperature change time length and a pre-stored heat conduction oil heat calculation formula.

309: and the biochemical degradation equipment adjusts the working power of the heat conduction oil control module to be the first working power so as to obtain that the temperature in the biochemical degradation equipment cabin is in a set temperature range.

It should be noted that, the specific implementation of the steps of the method shown in fig. 3 can refer to the specific implementation described in the above method, and will not be described here.

Referring to fig. 4, fig. 4 is a block diagram illustrating functional units of a biochemical degradation apparatus 400 according to an embodiment of the present application, where the biochemical degradation apparatus includes:

a first obtaining unit 401, configured to obtain a current temperature in the biochemical degradation equipment compartment;

a first determining unit 402, configured to determine a temperature difference between the current temperature and a set critical temperature if the current temperature is greater than or equal to the set critical temperature;

a second determining unit 403 for determining at least one temperature control module based on the temperature difference value;

the adjusting unit 404 is configured to adjust the temperature in the biochemical degradation equipment compartment by using a preset temperature control method based on the at least one temperature control module, so as to obtain that the temperature in the biochemical degradation equipment compartment is within a set temperature range.

It can be seen that, in the embodiment of the present application, when the current temperature in the biochemical degradation equipment chamber is greater than or equal to the set critical temperature, the biochemical degradation equipment determines at least one temperature control module based on a temperature difference between the current temperature and the set critical temperature, and adjusts the temperature in the biochemical degradation equipment chamber by using a preset temperature control method based on the at least one temperature control module. Compare in biochemical degradation equipment control heating rod repeated heating conduction oil lead to the temperature in biochemical degradation equipment cabin can't be stabilized in a certain temperature range for a long time, this application embodiment can realize when biochemical degradation equipment is in operating condition for the temperature in biochemical degradation equipment cabin is in the settlement temperature range, helps improving rubbish degradation efficiency.

In one possible example, the at least one temperature control module includes a thermal oil control module and a degradation agent control module, and the adjusting unit 404 is specifically configured to, in terms of adjusting the temperature in the biochemical degradation equipment chamber by using a preset temperature control method based on the at least one temperature control module:

determining a first heat corresponding to the temperature difference value based on a pre-stored heat-temperature calculation formula;

acquiring a first temperature change rate in the biochemical degradation equipment cabin, and determining a first temperature change duration based on the first temperature change rate and the temperature difference;

acquiring a first degradation agent weight corresponding to the degradation agent control module and the current working power of the heat conduction oil control module, and determining a second heat corresponding to the degradation agent control module based on the first degradation agent weight, the temperature difference value, the first temperature change time length and a prestored degradation agent heat calculation formula;

determining a first heat difference value between the first heat and the second heat, and determining a first working power adjusted by the heat conduction oil control module based on the first heat difference value, the current working power of the heat conduction oil control module, the first temperature change time length and a pre-stored heat conduction oil heat calculation formula;

and adjusting the working power of the heat conduction oil control module to be the first working power.

In one possible example, the at least one temperature control module includes a hot air control module, a water vapor condensation control module, and a degradation agent control module, and the adjusting unit 403 is specifically configured to, in terms of adjusting the temperature in the biochemical degradation equipment chamber based on the at least one temperature control module by using a preset temperature control method:

determining a third heat corresponding to the temperature difference value based on the heat-temperature calculation formula;

acquiring a second temperature change rate in the biochemical degradation equipment cabin, and determining a second temperature change duration based on the second temperature change rate and the temperature difference;

obtaining a second degradation agent weight corresponding to the degradation agent control module and the current working power of the hot air control module, and determining a fourth heat corresponding to the degradation agent control module based on the second degradation agent weight, the temperature difference value, the second temperature change time length and the degradation agent heat calculation formula;

determining a second heat difference value of the third heat and the fourth heat, and acquiring a second working power adjusted by the hot air control module based on the second heat difference value, the current working power of the hot air control module, the second temperature change time length and a pre-stored hot air-steam heat calculation formula;

and adjusting the working power of the hot air control module to be the second working power.

In a possible example, the at least one temperature control module includes a garbage stirring control module and a degrading agent control module, and the adjusting unit 404 is specifically configured to, in terms of adjusting the temperature in the biochemical degradation equipment chamber by using a preset temperature control method based on the at least one temperature control module:

determining a fifth heat corresponding to the temperature difference value based on the heat-temperature calculation formula;

acquiring a third temperature change rate in the biochemical degradation equipment cabin, and determining a third temperature change duration based on the third temperature change rate and the temperature difference;

acquiring a third degradation agent weight corresponding to the degradation agent control module and the current working power of the garbage stirring control module, and determining a sixth heat corresponding to the degradation agent control module based on the third degradation agent weight, the temperature difference, the third temperature change time length and the degradation agent heat calculation formula;

determining a third heat difference value between the fifth heat and the sixth heat, and determining a third working power adjusted by the garbage stirring control module based on the third heat difference value, the current working power of the garbage stirring control module, the third temperature change time length and a prestored stirring heat calculation formula;

and adjusting the working power of the garbage stirring control module to be the third working power.

In one possible example, the at least one temperature control module includes a heat conducting oil control module, a hot air control module, a water vapor condensation control module, and a degradation agent control module, and in terms of adjusting the temperature in the biochemical degradation equipment chamber based on the at least one temperature control module by using a preset temperature control method, the adjusting unit 404 is specifically configured to:

determining a seventh heat corresponding to the temperature difference value based on the heat-temperature calculation formula;

acquiring a fourth temperature change rate in the biochemical degradation equipment cabin, and determining a fourth temperature change duration based on the fourth temperature change rate and the temperature difference;

acquiring a fourth degradation agent weight corresponding to the degradation agent control module, the current working power of the heat transfer oil control module and the current working power of the hot air control module, and determining an eighth heat corresponding to the degradation agent control module based on the fourth degradation agent weight, the temperature difference, the fourth temperature change time and the degradation agent heat calculation formula;

determining a fourth heat difference value between the seventh heat and the eighth heat, and determining a ninth heat corresponding to the heat-conducting oil control module based on the fourth heat difference value and a first proportion corresponding to the heat-conducting oil control module;

determining fourth working power adjusted by the heat conduction oil control module based on the ninth heat, the current working power of the heat conduction oil control module and the fourth temperature change duration;

determining a fifth heat difference value between the fourth heat difference value and the ninth heat, and acquiring a fifth working power adjusted by the hot air control module based on the fifth heat difference value, the current working power of the hot air control module, the fourth temperature change time length and the hot air-steam heat calculation formula;

and adjusting the working power of the heat conduction oil control module to be the fourth working power, and adjusting the working power of the hot air control module to be the fifth working power.

In one possible example, the biochemical degradation apparatus 400 further includes a second obtaining unit 405 and a third determining unit 406, wherein:

a second obtaining unit 405, configured to obtain a target temperature change rate in the biochemical degradation equipment compartment if the current temperature is greater than or equal to the set critical temperature;

a third determining unit 406 for determining the at least one temperature control module based on the target temperature change rate;

the adjusting unit 404 is further configured to adjust the temperature in the biochemical degradation equipment compartment by using the preset temperature control method based on the at least one temperature control module, so as to obtain that the temperature in the biochemical degradation equipment compartment is within the set temperature range.

In accordance with the embodiments shown in fig. 2 and fig. 3, referring to fig. 5, fig. 5 is a schematic structural diagram of another biodegradation apparatus provided in the embodiments of the present application, the biodegradation apparatus 500 includes a processor, a memory, a communication interface, and one or more programs, the one or more programs are stored in the memory and configured to be executed by the processor, and the programs include instructions for performing the following steps:

It can be seen that, in the embodiment of the present application, when the current temperature in the biochemical degradation equipment chamber is greater than or equal to the set critical temperature, the biochemical degradation equipment determines the at least one temperature control module based on a temperature difference between the current temperature and the set critical temperature, and adjusts the temperature range in the biochemical degradation equipment chamber by using a preset temperature control method based on the at least one temperature control module. Compare in biochemical degradation equipment control heating rod repeated heating conduction oil lead to the temperature in biochemical degradation equipment cabin can't be stabilized in a certain temperature range for a long time, this application embodiment can realize when biochemical degradation equipment is in operating condition for the temperature in biochemical degradation equipment cabin is in the settlement temperature range, helps improving rubbish degradation efficiency.

In one possible example, the at least one temperature control module comprises a thermal oil control module and a degradation agent control module, and the program comprises instructions for performing the following steps in particular in terms of adjusting the temperature in the biochemical degradation equipment compartment based on the at least one temperature control module by using a preset temperature control method:

In one possible example, the at least one temperature control module comprises a hot air control module, a water vapor condensation control module, and a degradation agent control module, the program comprising instructions specifically configured to perform the following steps in adjusting the temperature within the biochemical degradation equipment compartment using a preset temperature control method based on the at least one temperature control module:

In one possible example, the at least one temperature control module comprises a waste mixing control module and a degrading agent control module, and the program comprises instructions specifically for performing the following steps in adjusting the temperature in the biochemical degradation equipment compartment based on the at least one temperature control module using a preset temperature control method:

In one possible example, the at least one temperature control module comprises a heat transfer oil control module, a hot air control module, a water vapor condensation control module, and a degradation agent control module, and the program comprises instructions specifically configured to perform the following steps in adjusting the temperature in the biochemical degradation equipment compartment based on the at least one temperature control module using a preset temperature control method:

In one possible example, the program further includes instructions for performing the steps of:

if the current temperature is greater than or equal to the set critical temperature, acquiring a target temperature change rate in the biochemical degradation equipment cabin;

determining the at least one temperature control module based on the target rate of temperature change;

and adjusting the temperature in the biochemical degradation equipment cabin by adopting the preset temperature control method based on the at least one temperature control module to obtain that the temperature in the biochemical degradation equipment cabin is in the set temperature range.

Embodiments of the present application also provide a computer storage medium for storing a computer program for electronic data exchange, the computer program enabling a computer to perform part or all of the steps of any one of the methods as described in the above method embodiments, the computer including a biochemical degradation device.

Embodiments of the present application also provide a computer program product comprising a non-transitory computer readable storage medium storing a computer program operable to cause a computer to perform some or all of the steps of any of the methods as described in the above method embodiments. The computer program product may be a software installation package, said computer comprising biochemical degradation equipment.

It should be noted that, for simplicity of description, the above-mentioned method embodiments are described as a series of acts or combination of acts, but those skilled in the art will recognize that the present application is not limited by the order of acts described, as some steps may occur in other orders or concurrently depending on the application. Further, those skilled in the art should also appreciate that the embodiments described in the specification are preferred embodiments and that the acts and modules referred to are not necessarily required in this application.

In the foregoing embodiments, the descriptions of the respective embodiments have respective emphasis, and for parts that are not described in detail in a certain embodiment, reference may be made to related descriptions of other embodiments.

In the embodiments provided in the present application, it should be understood that the disclosed apparatus may be implemented in other manners. For example, the above-described embodiments of the apparatus are merely illustrative, and for example, the above-described division of the units is only one type of division of logical functions, and other divisions may be realized in practice, for example, a plurality of units or components may be combined or integrated into another system, or some features may be omitted, or not executed. In addition, the shown or discussed mutual coupling or direct coupling or communication connection may be an indirect coupling or communication connection of some interfaces, devices or units, and may be an electric or other form.

The units described as separate parts may or may not be physically separate, and parts displayed as units may or may not be physical units, may be located in one place, or may be distributed on a plurality of network units. Some or all of the units can be selected according to actual needs to achieve the purpose of the solution of the embodiment.

In addition, functional units in the embodiments of the present application may be integrated into one processing unit, or each unit may exist alone physically, or two or more units are integrated into one unit. The integrated unit can be realized in a form of hardware, and can also be realized in a form of a software functional unit.

The integrated unit may be stored in a computer readable memory if it is implemented in the form of a software functional unit and sold or used as a stand-alone product. Based on such understanding, the technical solution of the present application may be substantially implemented or a part of or all or part of the technical solution contributing to the prior art may be embodied in the form of a software product stored in a memory, and including several instructions for causing a computer device (which may be a personal computer, a server, or a network device) to execute all or part of the steps of the above-mentioned method of the embodiments of the present application. And the aforementioned memory comprises: a U-disk, a Read-Only Memory (ROM), a Random Access Memory (RAM), a removable hard disk, a magnetic or optical disk, and other various media capable of storing program codes.

Those skilled in the art will appreciate that all or part of the steps in the methods of the above embodiments may be implemented by associated hardware instructed by a program, which may be stored in a computer-readable memory, which may include: flash Memory disks, Read-Only memories (ROMs), Random Access Memories (RAMs), magnetic or optical disks, and the like.

The foregoing detailed description of the embodiments of the present application has been presented to illustrate the principles and implementations of the present application, and the above description of the embodiments is only provided to help understand the method and the core concept of the present application; meanwhile, for a person skilled in the art, according to the idea of the present application, there may be variations in the specific implementation and application scope, and in view of the above, the content of the present specification should not be construed as a limitation to the present application.

Claims

1. The thermal balance control method is characterized by being applied to biochemical degradation equipment, wherein the biochemical degradation equipment comprises a cabin body, a cabin cover arranged on the upper side of the cabin body, a garbage can traction system and a condensation port arranged on the side edge of the cabin body, a water vapor drainage system and a condensation system arranged on the condensation port, a degradation tank arranged in the cabin body, a stirring system and a degrading agent feeding device arranged in a degradation tank area, a heat conduction oil heating system arranged in the degradation tank area and a hot air device arranged in the cabin body, garbage to be degraded poured through the garbage can traction system and the feeding port of the cabin cover is arranged in the degradation tank, and the method comprises the following steps:

2. The method according to claim 1, wherein the at least one temperature control module comprises a thermal oil control module and a degradation agent control module, and the adjusting the temperature in the biochemical degradation equipment chamber based on the at least one temperature control module by adopting a preset temperature control method comprises:

3. The method of claim 1, wherein the at least one temperature control module comprises a hot air control module, a water vapor condensation control module, and a degradation agent control module, and wherein adjusting the temperature within the biochemical degradation plant compartment based on the at least one temperature control module using a predetermined temperature control method comprises:

4. The method of claim 1, wherein the at least one temperature control module comprises a waste mixing control module and a degradation agent control module, and the adjusting the temperature in the biochemical degradation equipment compartment based on the at least one temperature control module using a preset temperature control method comprises:

5. The method according to claim 1, wherein the at least one temperature control module comprises a conduction oil control module, a hot air control module, a water vapor condensation control module and a degradation agent control module, and the adjusting the temperature in the biochemical degradation equipment chamber based on the at least one temperature control module by adopting a preset temperature control method comprises:

6. The method of claim 1, further comprising:

7. The utility model provides a biochemical degradation equipment, its characterized in that, biochemical degradation equipment include the cabin body, set up in the cabin cover of cabin body upside, set up in garbage bin traction system and the condensation port of cabin body side, set up in the vapor drainage system and the condensation system of condensation port, set up in the inside degradation groove of cabin body, set up in the regional mixing system of degradation groove and degradation agent throw the material device, set up in the regional conduction oil heating system of degradation groove with set up in the hot blast apparatus of the cabin body, be equipped with in the degradation groove through garbage bin traction system with the waiting to degrade rubbish that the pan feeding mouth of cabin cover emptys, equipment includes:

the first taking unit is used for obtaining the current temperature in the biochemical degradation equipment cabin;

8. The method according to claim 7, wherein the adjusting unit is specifically configured to, in adjusting the temperature in the biochemical degradation equipment compartment based on the at least one temperature control module using a preset temperature control method:

9. The method according to claim 7, wherein the adjusting unit is specifically configured to, in adjusting the temperature in the biochemical degradation equipment compartment based on the at least one temperature control module using a preset temperature control method:

10. A computer-readable storage medium, characterized in that the computer-readable storage medium is used to store a computer program, which is executed by a processor to implement the method according to any of claims 1-6.