CN111796612A

CN111796612A - Temperature control method and related product

Info

Publication number: CN111796612A
Application number: CN201910282015.4A
Authority: CN
Inventors: 吕胜军; 莫乙玟; 蒋晓明
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

Abstract

The embodiment of the application discloses a temperature control method and a related product, which are applied to biochemical degradation equipment, wherein the biochemical degradation equipment comprises a hot air pipe and a degradation groove; the method comprises the following steps: receiving a request for starting biochemical degradation treatment of the garbage, wherein the real-time temperature of the hot air pipe and the real-time temperature of the degradation tank are the real-time temperatures of the hot air pipe and the degradation tank; according to a preset degradation treatment temperature interval, performing temperature control operation to adjust the temperature of the inner space of the biochemical degradation equipment to be in the degradation treatment temperature interval; and performing biochemical degradation treatment on the garbage when the temperature of the inner space of the biochemical degradation equipment is within the degradation treatment temperature range. Therefore, in the application, the simplicity of operation during temperature control is ensured, the efficiency of temperature control is improved, the temperature control of biochemical degradation equipment is optimized, and the biochemical degradation of garbage is more convenient, effective, safe and environment-friendly.

Description

Temperature control method and related product

Technical Field

The application relates to the technical field of biochemical degradation equipment, in particular to a temperature control method and a related product.

Background

In daily life, a large amount of garbage is generated, and most of the garbage is subjected to landfill treatment or incineration treatment. A large amount of space is needed for landfill treatment, and land resources and social resources are greatly wasted; and a large amount of harmful smoke and gas can be generated by incineration treatment, so that the environment is damaged, the environment is greatly polluted, and the method is not suitable for the environmental protection concept.

Therefore, it is urgently needed to provide a garbage disposal apparatus and a control method thereof, which can effectively dispose and reasonably utilize the domestic garbage.

Disclosure of Invention

The embodiment of the application provides a temperature control method and a related product, so that the high efficiency and convenience of temperature control are expected to be improved.

In a first aspect, an embodiment of the present application provides a temperature control method, which is applied to a biochemical degradation apparatus, where the biochemical degradation apparatus includes a hot air duct and a degradation tank; the method comprises the following steps:

receiving a request for starting biochemical degradation treatment of garbage, and acquiring a real-time temperature of a hot air pipe and a real-time temperature of a degradation tank, wherein the real-time temperature of the hot air pipe is the temperature of the hot air pipe, and the real-time temperature of the degradation tank is the temperature of the degradation tank;

according to a preset degradation treatment temperature interval, performing temperature control operation to adjust the temperature of the inner space of the biochemical degradation equipment to be in the degradation treatment temperature interval, wherein the degradation treatment temperature interval is associated with a hot air pipe temperature interval and a degradation tank temperature interval, and the temperature of the inner space of the biochemical degradation equipment is associated with the real-time temperature of the hot air pipe and the real-time temperature of the degradation tank;

and performing biochemical degradation treatment on the garbage when the temperature of the inner space of the biochemical degradation equipment is within the degradation treatment temperature range.

In a second aspect, an embodiment of the present application provides a temperature control device, which is applied to a biochemical degradation apparatus, where the biochemical degradation apparatus includes a hot air duct and a degradation tank; the temperature control device comprises a processing unit and a communication unit, wherein,

the processing unit is used for receiving a request for starting biochemical degradation treatment of the garbage, and acquiring the real-time temperature of the hot air pipe and the real-time temperature of the degradation tank, wherein the real-time temperature of the hot air pipe is the temperature of the hot air pipe, and the real-time temperature of the degradation tank is the temperature of the degradation tank; the temperature control device is used for carrying out temperature control operation according to a preset degradation treatment temperature interval so as to adjust the temperature of the inner space of the biochemical degradation equipment to be in the degradation treatment temperature interval, wherein the degradation treatment temperature interval is related to a hot air pipe temperature interval and a degradation tank temperature interval, and the temperature of the inner space of the biochemical degradation equipment is related to the real-time temperature of the hot air pipe and the real-time temperature of the degradation tank; and the biochemical degradation treatment device is used for performing biochemical degradation treatment on the garbage when the temperature of the inner space of the biochemical degradation device is within the degradation treatment temperature range.

In a third aspect, embodiments of the present application provide a biochemical degradation apparatus, including a processor, a memory, a communication interface, and one or more programs, where the one or more programs are stored in the memory and configured to be executed by the processor, and the program includes instructions for performing steps in any of the methods of the first aspect of the embodiments of the present application.

In a fourth aspect, the present application provides a computer-readable storage medium, where the computer-readable storage medium stores a computer program for electronic data exchange, where the computer program makes a computer perform part or all of the steps described in any one of the methods in the second aspect of the present application.

In a fifth aspect, the present application provides a computer program product, wherein the computer program product includes a non-transitory computer-readable storage medium storing a computer program, and the computer program is operable to cause a computer to perform some or all of the steps described in any one of the methods of the second aspect 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, a temperature control method is provided, which is applied to a biochemical degradation apparatus, where the biochemical degradation apparatus includes a hot air duct and a degradation tank; the method comprises the following steps: receiving a request for starting biochemical degradation treatment of garbage, and acquiring a real-time temperature of a hot air pipe and a real-time temperature of a degradation tank, wherein the real-time temperature of the hot air pipe is the temperature of the hot air pipe, and the real-time temperature of the degradation tank is the temperature of the degradation tank; according to a preset degradation treatment temperature interval, performing temperature control operation to adjust the temperature of the inner space of the biochemical degradation equipment to be in the degradation treatment temperature interval; and performing biochemical degradation treatment on the garbage when the temperature of the inner space of the biochemical degradation equipment is within the degradation treatment temperature range. It can be seen that in this application, be in the degradation processing temperature interval through controlling hot-blast main real-time temperature and degradation groove real-time temperature, be favorable to improving temperature control's high efficiency and accuracy, be favorable to managers convenient and fast's control biochemical degradation equipment's temperature, the simplicity of operation when both having guaranteed temperature control has improved temperature control's efficiency again, has optimized biochemical degradation equipment's temperature control, makes rubbish biochemical degradation become more convenient effective, safety ring protects.

Drawings

In order to more clearly illustrate the embodiments of the present application or the technical solutions in the prior art, the drawings used in the description of the embodiments or the prior art will be briefly described below, it is obvious that the drawings in the following description are only some embodiments of the present application, and for those skilled in the art, other drawings can be obtained according to the drawings without creative efforts.

Fig. 1 is a schematic flow chart of a temperature control method provided in an embodiment of the present application;

FIG. 2a is a schematic structural diagram of a biochemical degradation apparatus provided in an embodiment of the present application;

FIG. 2b is a schematic structural diagram of another biochemical degradation apparatus provided in an embodiment of the present application;

FIG. 3 is a schematic structural diagram of a biochemical degradation apparatus provided in an embodiment of the present application;

fig. 4 is a block diagram of functional units of a temperature control device according to an embodiment of the present disclosure.

Detailed Description

In order to make the technical solutions of the present application better understood, 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 herein 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 application. 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.

The biochemical degradation equipment related to the embodiment of the application can comprise an equipment body provided with a feed port and a degradation groove which is arranged in the equipment body and communicated with the feed port; the feeding port of the equipment body is provided with a switchable feeding port, the equipment body is provided with a liftable conveying ladder, the equipment body is provided with a fan and is connected with a hot air pipe on the equipment body, the equipment body is also provided with a bottom heating system, at least one heating rod is used for heating heat conduction oil, and the constant temperature environment in the equipment is kept; and a touch display screen is also arranged on the outer surface of the equipment body.

A temperature control system is arranged in the equipment body; the temperature control system is connected with the touch display screen; a user can input a corresponding operation instruction to the temperature control system by operating on the touch display screen, the temperature control system can control corresponding components to react according to the received instruction, for example, the real-time temperature of the hot air pipe is controlled by controlling the air output of the fan, and/or the real-time temperature of the degradation tank is controlled by controlling the heating temperature of the bottom heating system, and the temperature control system can also display the real-time temperature of the hot air pipe and the real-time temperature of the degradation tank through the touch display screen; the degradation inslot is equipped with the (mixing) shaft, is fixed with at least one rabbling arm on the (mixing) shaft.

The following describes embodiments of the present application in detail.

Referring to fig. 1, fig. 1 is a schematic flow chart of a temperature control method applied to a biochemical degradation apparatus including a hot air duct and a degradation tank according to an embodiment of the present application; the method comprises the following steps:

s101, receiving a request for starting biochemical degradation treatment of garbage by biochemical degradation equipment, and acquiring the real-time temperature of a hot air pipe and the real-time temperature of a degradation tank;

the real-time temperature of the hot air pipe is the temperature of the hot air pipe, and the real-time temperature of the degradation tank is the temperature of the degradation tank;

s102, the biochemical degradation equipment performs temperature control operation according to a preset degradation treatment temperature interval so as to adjust the temperature of the inner space of the biochemical degradation equipment to be in the degradation treatment temperature interval;

the degradation treatment temperature interval is associated with a hot air pipe temperature interval and a degradation tank temperature interval, the hot air pipe temperature interval comprises an upper layer temperature interval which mainly limits the internal space of the biochemical degradation equipment, and the degradation tank temperature interval comprises a lower layer temperature interval which mainly limits the internal space of the biochemical degradation equipment;

the degradation treatment temperature interval is to maintain a stable constant temperature environment in the equipment, ensure that the activity of the degradation agent is strong in a certain temperature interval, evaporate water molecules, realize moisture isolation, convert the to-be-degraded substances into chemical fertilizers and ensure the conversion rate;

the temperature of the inner space of the biochemical degradation equipment is related to the real-time temperature of the hot air pipe and the real-time temperature of the degradation tank;

the control of the real-time temperature of the hot air pipe mainly refers to control of the upper layer temperature in the internal space of the biochemical degradation equipment, so that the internal space temperature of the biochemical degradation equipment is basically synchronous, and/or the evaporated water vapor cannot be condensed too early and then flows back to a garbage pile in the rising process in the garbage biochemical degradation process;

wherein, the real-time temperature of the degradation tank is mainly used for controlling the temperature of the lower layer in the internal space of the biochemical degradation equipment, so that the temperature of the internal space of the biochemical degradation equipment is basically synchronous, and the temperature of the part is controlled by a diversified adjusting mode;

s103, performing biochemical degradation treatment on the garbage by the biochemical degradation equipment when the temperature of the inner space of the biochemical degradation equipment is within the degradation treatment temperature range.

In one possible example, the performing the temperature control operation to adjust the temperature of the internal space of the biochemical degradation apparatus to be in the degradation process temperature interval according to the preset degradation process temperature interval includes: the biochemical degradation equipment determines a hot air pipe temperature interval of the hot air pipe and a degradation groove temperature interval of the degradation groove according to the preset degradation treatment temperature interval; the biochemical degradation equipment adjusts the real-time temperature of the hot air pipe according to the real-time temperature of the hot air pipe and the temperature interval of the hot air pipe, and determines that the real-time temperature of the hot air pipe is in the temperature interval of the hot air pipe; the biochemical degradation equipment adjusts the real-time temperature of the degradation tank according to the real-time temperature of the degradation tank and the temperature interval of the degradation tank, and the real-time temperature of the degradation tank is determined to be in the temperature interval of the degradation tank; and the biochemical degradation equipment acquires the adjusted real-time temperature of the hot air pipe and the adjusted real-time temperature of the degradation tank.

The degradation treatment temperature interval is related to the hot air pipe temperature interval and the degradation tank temperature interval, and the relationship is as follows: based on a preset mapping relation, corresponding relations exist between the degradation treatment temperature interval and the two temperature intervals respectively, and the preset mapping relation can be obtained based on prior data. In the concrete implementation, when the degradation agent is put into the degradation tank, the degradation agent is sprayed on the upper layer of the garbage to be degraded from top to bottom, the temperature range of the hot air pipe comprises an upper layer temperature range mainly used for adjusting and limiting the internal space of the biochemical degradation equipment, and the temperature range of the degradation tank comprises a lower layer temperature range mainly used for adjusting and limiting the internal space of the biochemical degradation equipment, namely, the degradation agent is firstly mainly influenced by the temperature of the upper layer space, namely the hot air pipe, and is gradually mixed into the internal or bottom layer space along with the stirring of the biochemical degradation equipment by the stirring device, so that the degradation agent is gradually influenced by the heating device of the degradation tank to further increase the temperature, and finally reaches a better degradation treatment temperature range, and the processes can be seen that the degradation agent is required to be mixed with the garbage to be treated on the one hand, and the temperature is required to rapidly increase to the degradation treatment temperature range on the other hand, therefore, the temperature of the hot air pipe can be slightly lower than the heating temperature of the heating device, and because the hot air pipe is not completely mixed at this stage, even if the temperature is very high, the influence on the degradation efficiency is small, after a certain time, the degradation agent and the garbage to be treated are completely mixed, more of the degradation agent is influenced by the temperature at the bottom of the biochemical degradation equipment, and the temperature in the degradation tank is in a degradation treatment temperature range at the moment, so that the activity of the degradation agent is favorably ensured, and the higher degradation efficiency is ensured.

The temperature of the inner space of the biochemical degradation equipment is related to the real-time temperature of the hot air pipe and the real-time temperature of the degradation tank, the real-time temperature of the hot air pipe comprises the upper layer temperature of the inner space of the main control biochemical degradation equipment, the real-time temperature of the degradation tank comprises the lower layer temperature of the inner space of the main control biochemical degradation equipment, and the degradation treatment temperature of the degradation tank can be comprehensively controlled through the temperature synthesis of the two spaces.

The biochemical degradation equipment obtains the adjusted real-time temperature of the hot air pipe and the real-time temperature of the degradation tank and comprises the following steps: and the biochemical degradation equipment continuously acquires the adjusted real-time temperature of the hot air pipe and the real-time temperature of the degradation tank, and if the acquired real-time temperature of the hot air pipe and the real-time temperature of the degradation tank are not in the temperature range of the hot air pipe and the temperature range of the degradation tank, the temperature control operation is carried out again until the biochemical degradation treatment of the garbage is finished.

In the concrete implementation, the biochemical degradation equipment acquires that the real-time temperature of the hot air pipe is 50 ℃, and if the temperature interval of the hot air pipe is 55-80 ℃, the real-time temperature of the hot air pipe is adjusted to be 60 ℃, and the real-time temperature of the hot air pipe is determined to be within 55-80 ℃ of the temperature interval of the hot air pipe; the real-time temperature of the degradation tank is 65 ℃, and the known temperature interval of the degradation tank is 60-90 ℃, so that the real-time temperature of the degradation tank does not need to be adjusted, and the real-time temperature of the degradation tank is determined to be within 60-90 ℃ of the temperature interval of the degradation tank; and the biochemical degradation equipment obtains the adjusted real-time temperature of the hot air pipe of 60 ℃ and the real-time temperature of the degradation tank of 65 ℃.

In the concrete implementation, the biochemical degradation equipment acquires that the real-time temperature of the hot air pipe is 50 ℃, and if the temperature interval of the hot air pipe is 55-80 ℃, the real-time temperature of the hot air pipe is adjusted to be 60 ℃, and the real-time temperature of the hot air pipe is determined to be within 55-80 ℃ of the temperature interval of the hot air pipe; the real-time temperature of the degradation tank is 97 ℃, and if the temperature interval of the degradation tank is known to be 60-90 ℃, the real-time temperature of the degradation tank is adjusted to 88, and the real-time temperature of the degradation tank is determined to be within 60-90 ℃ of the temperature interval of the degradation tank; the biochemical degradation equipment obtains the adjusted real-time temperature of the hot air pipe of 60 ℃ and the real-time temperature of the degradation tank of 88 ℃; after a period of time, the biochemical degradation equipment acquires that the real-time temperature of the hot air pipe is changed to 85 ℃ and the real-time temperature of the degradation tank is 95 ℃, and then the real-time temperature of the hot air pipe and the real-time temperature of the degradation tank are adjusted again.

In this example, the biochemical degradation device adjusts the real-time temperature of the hot air pipe according to the real-time temperature of the hot air pipe and the temperature interval of the hot air pipe, and determines that the real-time temperature of the hot air pipe is within the temperature interval of the hot air pipe; adjusting the real-time temperature of the degradation tank according to the real-time temperature of the degradation tank and the temperature interval of the degradation tank, and determining that the real-time temperature of the degradation tank is in the temperature interval of the degradation tank; and finally, acquiring the adjusted real-time temperature of the hot air pipe and the adjusted real-time temperature of the degradation tank. The temperature of biochemical degradation equipment is controlled more stably, so that the inside of the equipment can be kept in a preset constant temperature environment, the degradation agent is guaranteed to have stronger activity under the constant temperature environment state, and meanwhile, water molecules are evaporated under the temperature environment, so that moisture isolation is realized, and the high-efficiency conversion rate of biochemical degradation of garbage is improved.

In one possible example, the biochemical degradation apparatus further includes a fan, and the adjusting the real-time temperature of the hot air duct according to the real-time temperature of the hot air duct and the temperature interval of the hot air duct to determine that the real-time temperature of the hot air duct is within the temperature interval of the hot air duct includes: according to the real-time temperature of the hot air pipe and the temperature interval of the hot air pipe, the biochemical degradation equipment determines that the real-time temperature of the hot air pipe is higher than the upper limit temperature of the temperature interval of the hot air pipe; the biochemical degradation equipment reduces the air output of the fan, and reduces the temperature of the hot air pipe in real time to the temperature range of the hot air pipe within a first time threshold.

Wherein, the fan is including being used for controlling the air output.

Wherein, air output includes the influence temperature and atmospheric pressure in the hot-blast pipe.

The hot air pipe is used for conveying hot air exhausted by the fan, the hot air pipe comprises a plurality of rotating parts, each rotating part can independently control and rotate independently, so that the hot air direction entering the interior of the biochemical degradation equipment is controlled, and meanwhile, each rotating part comprises an air outlet valve which is opened and closed to control the size of the hot air entering the interior of the biochemical degradation equipment.

In the specific implementation, according to the obtained real-time temperature of the hot air pipe being 82 ℃ and the known temperature interval of the hot air pipe being 55-80 ℃, the biochemical degradation equipment determines that the real-time temperature of the hot air pipe is 82 ℃ higher than the upper limit temperature of the temperature interval of the hot air pipe by 80 ℃; and if the first time threshold is known to be 5 minutes, the biochemical degradation equipment reduces the real-time temperature of the hot air pipe to the temperature interval of the hot air pipe within 5 minutes by reducing the air output of the fan.

In this example, the biochemical degradation device determines that the real-time temperature of the hot air pipe is higher than the upper limit temperature of the temperature interval of the hot air pipe according to the real-time temperature of the hot air pipe and the temperature interval of the hot air pipe; through reducing the air output of fan reduces in the threshold value of the very first time the real-time temperature of hot-blast main arrives in the hot-blast main temperature interval to carry out temperature control, avoid because the equipment that the real-time temperature of hot-blast main too high caused damages or accident, be favorable to improving temperature control's high efficiency and convenience, make the constancy of temperature effectively in the degradation treatment temperature interval of predetermineeing, be favorable to improving biochemical degradation efficiency.

In one possible example, the biochemical degradation apparatus further includes a fan, and the adjusting the real-time temperature of the hot air duct according to the real-time temperature of the hot air duct and the temperature interval of the hot air duct to determine that the real-time temperature of the hot air duct is within the temperature interval of the hot air duct includes: according to the real-time temperature of the hot air pipe and the temperature interval of the hot air pipe, the biochemical degradation equipment determines that the real-time temperature of the hot air pipe is lower than the lower limit temperature of the temperature interval of the hot air pipe; and the biochemical degradation equipment increases the air outlet measurement of the fan, and raises the real-time temperature of the hot air pipe to the temperature range of the hot air pipe within a second time threshold.

In the specific implementation, according to the fact that the obtained real-time temperature of the hot air pipe is 50 ℃ and the known temperature interval of the hot air pipe is 55-80 ℃, the biochemical degradation equipment determines that the real-time temperature of the hot air pipe is 50 ℃ lower than the lower limit temperature of the temperature interval of the hot air pipe by 55 ℃; and if the second time threshold is known to be 6 minutes, the biochemical degradation equipment raises the real-time temperature of the hot air pipe to the temperature interval of the hot air pipe within 6 minutes by increasing the air output of the fan.

In this example, the biochemical degradation device determines that the real-time temperature of the hot air pipe is lower than the lower limit temperature of the temperature interval of the hot air pipe according to the real-time temperature of the hot air pipe and the temperature interval of the hot air pipe; through the increase the air output of fan risees in the second time threshold the hot-blast main real-time temperature arrives in the hot-blast main temperature interval to carry out temperature control, avoid because the hot-blast main real-time temperature crosses low biochemical degradation efficiency that causes and hang down or accident excessively, be favorable to improving temperature control's high efficiency and convenience, make the constancy of temperature effectively in predetermined degradation treatment temperature interval, be favorable to improving biochemical degradation efficiency.

In one possible example, the biochemical degradation apparatus further includes at least one heating rod, and the adjusting the degradation tank real-time temperature according to the degradation tank real-time temperature and the degradation tank temperature interval, and determining that the degradation tank real-time temperature is within the degradation tank temperature interval includes: according to the real-time temperature of the degradation tank and the temperature interval of the degradation tank, the biochemical degradation equipment determines that the real-time temperature of the degradation tank is higher than the upper limit temperature of the temperature interval of the degradation tank; and the biochemical degradation equipment reduces the temperature of the at least one heating rod, and reduces the real-time temperature of the degradation tank to the temperature range of the degradation tank within a third time threshold.

Wherein, be provided with a plurality of heating device in the degradation inslot, heating rod and conduction oil can be established to every heating device, and the conduction oil makes heating device temperature rise through the heating rod heating, realizes heating the rubbish of waiting to decompose of the corresponding region in the degradation inslot. Wherein, this a plurality of heating device can be laid in the degradation groove bottom in the subregion, can also lay simultaneously in the degradation groove and be close to the side of bottom for the cooperation realizes treating degradation rubbish and heats.

In a specific implementation, as shown in fig. 2a, the plurality of heating devices may be laid on the bottom of the degradation tank in a partitioned manner, each heating device may be regarded as a heating partition, each heating partition includes at least one heating rod, and the at least one heating rod may work synchronously or asynchronously, so as to achieve the purpose of adjusting the real-time temperature of the degradation tank, and specifically, perform dynamic regulation and control according to needs.

Specifically, the real-time temperature of the degradation tank can be regulated and controlled, all heating devices are started when the real-time temperature of the degradation tank is obtained to be in a first temperature interval, and part of heating devices are started when the real-time temperature of the degradation tank is in a second temperature interval;

specifically, the control is carried out based on the real-time temperature of the degradation tank and the garbage distribution condition, the plurality of heating devices can be paved at the bottom of the degradation tank in a partitioned mode, each heating device can be regarded as a heating partition, and when the real-time temperature of the degradation tank is obtained to be in a first temperature interval and the garbage is uniformly distributed, the heating devices of all the heating partitions are started at the same time; when the temperature of the degradation tank is in a first temperature range and more garbage is in a first heating subarea, reducing the heating power of heating devices in the heating subareas except the first heating subarea and reducing the real-time temperature of the degradation tank; when the real-time temperature of the degradation tank is in a second temperature interval and more garbage is in a first heating subarea, increasing the heating power of a heating device in the first heating subarea and increasing the real-time temperature of the degradation tank; in a specific implementation, as shown in fig. 2B, it is assumed that A, B, C, D four heating partitions are arranged at the bottom of the degradation tank, and in the biochemical degradation process of the garbage, if it is determined that the amounts of the garbage in partition a and partition B are large, the two partitions can be preferentially heated;

specifically, determining a regulation temperature to regulate based on garbage recognition and analysis, analyzing and identifying garbage to be degraded, and adjusting the temperature of at least one heating rod according to an analysis and identification result and a preset temperature strategy in a database, wherein the preset temperature strategy comprises inquiring a preset mapping relation by using the analysis and identification result as an inquiry identifier to obtain a target temperature corresponding to the analysis and identification result, and the mapping relation comprises a corresponding relation between the analysis and identification result and the target temperature; or, according to the analysis and identification result, the real-time temperature of the degradation tank is controlled by artificially setting the heating power of the heating rod. In the concrete implementation, the content of the corn in the garbage biochemical degradation process is determined to be high based on video analysis and recognition, then a database is inquired to accurately determine the target temperature, and the heating power of the heating rod is controlled to enable the real-time temperature of the degradation tank to reach the target temperature.

In the specific implementation, according to the fact that the obtained real-time temperature of the degradation tank is 92 ℃ and the known temperature interval of the degradation tank is 60-90 ℃, the biochemical degradation equipment determines that the real-time temperature of the degradation tank is 92 ℃ higher than the upper limit temperature of the temperature interval of the degradation tank by 90 ℃; and if the third time threshold is 5 minutes, the biochemical degradation equipment reduces the temperature of the at least one heating rod within 5 minutes to reduce the real-time temperature of the hot air pipe to the temperature interval of the hot air pipe.

In this example, the biochemical degradation device determines that the real-time temperature of the degradation tank is higher than the upper limit temperature of the temperature interval of the degradation tank according to the real-time temperature of the degradation tank and the temperature interval of the degradation tank; and reducing the real-time temperature of the degradation tank to the temperature interval of the degradation tank within a third time threshold by reducing the temperature of the at least one heating rod. The device is beneficial to more efficiently and accurately controlling the real-time temperature of the degradation tank, avoids equipment damage or sudden accidents caused by overhigh real-time temperature of the degradation tank, improves the safety of the biochemical degradation equipment in the using process, effectively keeps the constant temperature in a preset degradation treatment temperature range, and ensures the biochemical degradation efficiency.

In one possible example, the biochemical degradation apparatus further includes at least one heating rod, and the adjusting the degradation tank real-time temperature according to the degradation tank real-time temperature and the degradation tank temperature interval, and determining that the degradation tank real-time temperature is within the degradation tank temperature interval includes: biochemical degradation equipment is used for carrying out real-time temperature control on the degradation tank and the temperature interval of the degradation tank; and the biochemical degradation equipment raises the temperature of the at least one heating rod, and raises the real-time temperature of the degradation tank to the temperature range of the degradation tank within a fourth time threshold.

The at least one heating rod is used for heating heat conducting oil laid on the bottom layer of the equipment, so that the real-time temperature of the degradation tank is controlled.

In the specific implementation, according to the obtained degradation tank real-time temperature of 55 ℃ and the known degradation tank temperature interval of 60-90 ℃, the biochemical degradation equipment determines that the degradation tank real-time temperature of 55 ℃ is lower than the lower limit temperature of 60 ℃ of the degradation tank temperature interval; and when the fourth time threshold is known to be 7 minutes, the biochemical degradation equipment raises the real-time temperature of the hot air pipe to the temperature interval of the hot air pipe within 7 minutes by raising the temperature of the at least one heating rod.

In this example, the biochemical degradation device determines that the real-time temperature of the degradation tank is lower than the lower limit temperature of the temperature interval of the degradation tank according to the real-time temperature of the degradation tank and the temperature interval of the degradation tank; increasing the temperature of the degradation tank real-time temperature to be within the degradation tank temperature interval within a fourth time threshold by increasing the temperature of the at least one heating rod. The device is beneficial to more efficiently and accurately controlling the real-time temperature of the degradation tank, avoids sudden accidents or excessively low biochemical degradation efficiency caused by excessively low real-time temperature of the degradation tank, improves the safety of biochemical degradation equipment in the using process, effectively keeps the constant temperature within a preset degradation treatment temperature range, and ensures the biochemical degradation efficiency.

In one possible example, the biochemical degradation apparatus further includes a touch display screen, and the temperature control operation is performed to adjust the temperature of the internal space of the biochemical degradation apparatus to be within the degradation processing temperature range according to a preset degradation processing temperature range, and the method further includes: adjusting the real-time temperature of the hot air pipe and/or the real-time temperature of the degradation tank by biochemical degradation equipment; the biochemical degradation equipment determines that the real-time temperature of the degradation tank is not in the temperature interval of the degradation tank within a certain time threshold, and/or the real-time temperature of the hot air pipe is not in the hot air temperature interval; the biochemical degradation equipment gives out early warning to managers and suspends the biochemical degradation treatment of the garbage.

Wherein, biochemical degradation equipment sends the early warning to managers, and the biochemical degradation of rubbish is handled to pause includes the following steps: the biochemical degradation equipment sends out sound early warning to corresponding equipment of the manager, and the temperature control fault is displayed on the touch display screen; and stopping the biochemical degradation treatment of the garbage by the biochemical degradation equipment, and waiting for the fault removal treatment by the manager.

In the specific implementation, the biochemical degradation equipment adjusts the real-time temperature of the hot air pipe to 50 ℃, the given time threshold is 10 minutes, and the hot air temperature interval is 55-80 ℃; after 10 minutes, the real-time temperature of the hot air pipe is not in the temperature range of the degradation tank, and at the moment, the biochemical degradation equipment gives an early warning to managers, suspends the biochemical degradation treatment of the garbage, and waits for the managers to carry out fault removal treatment.

In the concrete implementation, the biochemical degradation equipment adjusts the real-time temperature of the hot air pipe to be 50 ℃, and the real-time temperature of the degradation tank is 70 ℃; knowing that the certain time threshold is 10 minutes, the hot air temperature interval is 55-80 ℃, and the degradation tank temperature interval is 60-90 ℃; after 10 minutes, the real-time temperature of the hot air pipe is not in the temperature range of the degradation tank, and at the moment, the biochemical degradation equipment gives an early warning to managers, suspends the biochemical degradation treatment of the garbage, and waits for the managers to carry out fault removal treatment.

In this example, the biochemical degradation device adjusts the real-time temperature of the hot air pipe and/or the real-time temperature of the degradation tank; the biochemical degradation equipment determines that the real-time temperature of the degradation tank is not in the temperature interval of the degradation tank within a certain time threshold, and/or the real-time temperature of the hot air pipe is not in the hot air temperature interval; the biochemical degradation equipment sends out the early warning to managers, suspends rubbish biochemical degradation processing, is favorable to taking place temperature control failure, and biochemical degradation equipment can't stop rubbish biochemical degradation processing in time when degrading the temperature control of inner space and handling in degradation processing temperature interval, waits for managers to handle, avoids because the bad consequence that temperature control trouble leads to, improves rubbish biochemical degradation processing's security and high efficiency.

In accordance with the embodiment shown in fig. 1, please refer to fig. 3, fig. 3 is a schematic structural diagram of a biochemical degradation apparatus 300 according to an embodiment of the present application, and as shown in the figure, the biochemical degradation apparatus 300 includes an application processor 310, a memory 320, a communication interface 330, and one or more programs 321, wherein the one or more programs 321 are stored in the memory 320 and configured to be executed by the application processor 310, and the one or more programs 321 include instructions for performing the following steps;

In one possible example, the temperature control operation is performed to adjust the temperature of the internal space of the biochemical degradation apparatus to be in the degradation process temperature interval according to a preset degradation process temperature interval, and the instructions in the program are specifically configured to perform the following operations: determining a hot air pipe temperature interval of the hot air pipe and a degradation groove temperature interval of the degradation groove according to the preset degradation treatment temperature interval; adjusting the real-time temperature of the hot air pipe according to the real-time temperature of the hot air pipe and the temperature interval of the hot air pipe, and determining that the real-time temperature of the hot air pipe is in the temperature interval of the hot air pipe; adjusting the real-time temperature of the degradation tank according to the real-time temperature of the degradation tank and the temperature interval of the degradation tank, and determining that the real-time temperature of the degradation tank is in the temperature interval of the degradation tank; and acquiring the adjusted real-time temperature of the hot air pipe and the adjusted real-time temperature of the degradation tank.

In one possible example, the adjusting the real-time temperature of the hot air duct according to the real-time temperature of the hot air duct and the temperature interval of the hot air duct determines that the real-time temperature of the hot air duct is within the temperature interval of the hot air duct, and the instructions in the program are specifically configured to perform the following operations: determining that the real-time temperature of the hot air pipe is higher than the upper limit temperature of the hot air pipe temperature interval according to the real-time temperature of the hot air pipe and the hot air pipe temperature interval; and reducing the air output of the fan, and reducing the temperature of the hot air pipe in real time to the temperature range of the hot air pipe within a first time threshold.

In one possible example, the adjusting the real-time temperature of the hot air duct according to the real-time temperature of the hot air duct and the temperature interval of the hot air duct determines that the real-time temperature of the hot air duct is within the temperature interval of the hot air duct, and the instructions in the program are specifically configured to perform the following operations: determining that the real-time temperature of the hot air pipe is lower than the lower limit temperature of the hot air pipe temperature interval according to the real-time temperature of the hot air pipe and the hot air pipe temperature interval; and increasing the air output of the fan, and increasing the real-time temperature of the hot air pipe to the temperature range of the hot air pipe within a second time threshold.

In one possible example, the real-time degradation tank temperature is adjusted according to the real-time degradation tank temperature and the degradation tank temperature interval, and the real-time degradation tank temperature is determined to be within the degradation tank temperature interval, and the instructions in the program are specifically configured to perform the following operations: determining that the real-time temperature of the degradation tank is higher than the upper limit temperature of the temperature interval of the degradation tank according to the real-time temperature of the degradation tank and the temperature interval of the degradation tank; and reducing the temperature of the at least one heating rod, and reducing the real-time temperature of the degradation tank to the temperature interval of the degradation tank within a third time threshold.

In one possible example, the real-time degradation tank temperature is adjusted according to the real-time degradation tank temperature and the degradation tank temperature interval, and the real-time degradation tank temperature is determined to be within the degradation tank temperature interval, and the instructions in the program are specifically configured to perform the following operations: determining that the real-time temperature of the degradation tank is lower than the lower limit temperature of the temperature interval of the degradation tank according to the real-time temperature of the degradation tank and the temperature interval of the degradation tank; and increasing the temperature of the at least one heating rod, and increasing the real-time temperature of the degradation tank within a fourth time threshold value to be within the temperature interval of the degradation tank.

In one possible example, the temperature control operation is performed to adjust the temperature of the internal space of the biochemical degradation apparatus to be in the degradation process temperature interval according to a preset degradation process temperature interval, and the instructions in the program are specifically configured to perform the following operations: adjusting the real-time temperature of the hot air pipe and/or the real-time temperature of the degradation tank; determining that the real-time temperature of the degradation tank is not in the degradation tank temperature interval within a certain time threshold, and/or the real-time temperature of the hot air pipe is not in the hot air temperature interval; and sending early warning to managers, and suspending the biochemical degradation treatment of the garbage.

The above description has introduced the solution of the embodiment of the present application mainly from the perspective of the method-side implementation process. It is understood that the biochemical degradation device includes corresponding hardware structures and/or software modules for performing the respective functions in order to realize the functions. Those of skill in the art will readily appreciate that the present application is capable of hardware or a combination of hardware and computer software implementing the various illustrative elements and algorithm steps described in connection with the embodiments provided herein. Whether a function is performed as hardware or computer software drives hardware depends upon the particular application and design constraints imposed on the solution. Skilled artisans may implement the described functionality in varying ways for each particular application, but such implementation decisions should not be interpreted as causing a departure from the scope of the present application.

The embodiments of the present application may perform functional unit division on the biochemical degradation device according to the above method examples, for example, each functional unit may be divided corresponding to each function, or two or more functions may be integrated into one processing 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. It should be noted that the division of the unit in the embodiment of the present application is schematic, and is only a logic function division, and there may be another division manner in actual implementation.

Fig. 4 is a block diagram showing functional units of a temperature control device 400 according to an embodiment of the present application. The temperature control device 400 is applied to a biochemical degradation apparatus, and includes a processing unit 401 and a communication unit 402, wherein,

the processing unit 401 is configured to receive a request for starting biochemical degradation processing of garbage, and obtain a real-time temperature of a hot air pipe and a real-time temperature of a degradation tank, where the real-time temperature of the hot air pipe is the temperature of the hot air pipe, and the real-time temperature of the degradation tank is the temperature of the degradation tank; the temperature control device is used for carrying out temperature control operation according to a preset degradation treatment temperature interval so as to adjust the temperature of the inner space of the biochemical degradation equipment to be in the degradation treatment temperature interval, wherein the degradation treatment temperature interval is related to a hot air pipe temperature interval and a degradation tank temperature interval, and the temperature of the inner space of the biochemical degradation equipment is related to the real-time temperature of the hot air pipe and the real-time temperature of the degradation tank; and the biochemical degradation treatment device is used for performing biochemical degradation treatment on the garbage when the temperature of the inner space of the biochemical degradation device is within the degradation treatment temperature range.

In a possible example, the temperature control operation is performed to adjust the temperature of the internal space of the biochemical degradation apparatus to be in the degradation processing temperature interval according to a preset degradation processing temperature interval, and the processing unit 401 is specifically configured to: determining a hot air pipe temperature interval of the hot air pipe and a degradation groove temperature interval of the degradation groove according to the preset degradation treatment temperature interval; adjusting the real-time temperature of the hot air pipe according to the real-time temperature of the hot air pipe and the temperature interval of the hot air pipe, and determining that the real-time temperature of the hot air pipe is in the temperature interval of the hot air pipe; adjusting the real-time temperature of the degradation tank according to the real-time temperature of the degradation tank and the temperature interval of the degradation tank, and determining that the real-time temperature of the degradation tank is in the temperature interval of the degradation tank; and acquiring the adjusted real-time temperature of the hot air pipe and the adjusted real-time temperature of the degradation tank.

In a possible example, the adjusting the real-time temperature of the hot air duct according to the real-time temperature of the hot air duct and the hot air duct temperature interval determines that the real-time temperature of the hot air duct is within the hot air duct temperature interval, and the processing unit 401 is specifically configured to: determining that the real-time temperature of the hot air pipe is higher than the upper limit temperature of the hot air pipe temperature interval according to the real-time temperature of the hot air pipe and the hot air pipe temperature interval; and reducing the air output of the fan, and reducing the temperature of the hot air pipe in real time to the temperature range of the hot air pipe within a first time threshold.

In a possible example, the adjusting the real-time temperature of the hot air duct according to the real-time temperature of the hot air duct and the hot air duct temperature interval determines that the real-time temperature of the hot air duct is within the hot air duct temperature interval, and the processing unit 401 is specifically configured to: determining that the real-time temperature of the hot air pipe is lower than the lower limit temperature of the hot air pipe temperature interval according to the real-time temperature of the hot air pipe and the hot air pipe temperature interval; and increasing the air output of the fan, and increasing the real-time temperature of the hot air pipe to the temperature range of the hot air pipe within a second time threshold.

In a possible example, the real-time temperature of the degradation tank is adjusted according to the real-time temperature of the degradation tank and the temperature interval of the degradation tank, and it is determined that the real-time temperature of the degradation tank is within the temperature interval of the degradation tank, and the processing unit 401 is specifically configured to: determining that the real-time temperature of the degradation tank is higher than the upper limit temperature of the temperature interval of the degradation tank according to the real-time temperature of the degradation tank and the temperature interval of the degradation tank; and reducing the temperature of the at least one heating rod, and reducing the real-time temperature of the degradation tank to the temperature interval of the degradation tank within a third time threshold.

In a possible example, the real-time temperature of the degradation tank is adjusted according to the real-time temperature of the degradation tank and the temperature interval of the degradation tank, and it is determined that the real-time temperature of the degradation tank is within the temperature interval of the degradation tank, and the processing unit 401 is specifically configured to: determining that the real-time temperature of the degradation tank is lower than the lower limit temperature of the temperature interval of the degradation tank according to the real-time temperature of the degradation tank and the temperature interval of the degradation tank; and increasing the temperature of the at least one heating rod, and increasing the real-time temperature of the degradation tank within a fourth time threshold value to be within the temperature interval of the degradation tank.

In a possible example, the temperature control operation is performed to adjust the temperature of the internal space of the biochemical degradation apparatus to be in the degradation treatment temperature interval according to a preset degradation treatment temperature interval, and the method further includes the processing unit 401 specifically configured to: adjusting the real-time temperature of the hot air pipe and/or the real-time temperature of the degradation tank; determining that the real-time temperature of the degradation tank is not in the degradation tank temperature interval within a certain time threshold, and/or the real-time temperature of the hot air pipe is not in the hot air temperature interval; and sending early warning to managers, and suspending the biochemical degradation treatment of the garbage.

Embodiments of the present application also provide a computer storage medium, where the computer storage medium stores a computer program for electronic data exchange, the computer program enabling a computer to execute part or all of the steps of any one of the methods described in the above method embodiments, and the computer includes an electronic 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, the computer comprising an electronic device.

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 embodiments and the application scope, and in summary, the content of the present specification should not be construed as a limitation to the present application.

Claims

1. A temperature control method is characterized by being applied to biochemical degradation equipment, wherein the biochemical degradation equipment comprises a hot air pipe and a degradation groove; the method comprises the following steps:

2. The method according to claim 1, wherein the performing the temperature control operation to adjust the temperature of the internal space of the biochemical degradation apparatus to be in the degradation process temperature interval according to a preset degradation process temperature interval comprises:

determining a hot air pipe temperature interval of the hot air pipe and a degradation groove temperature interval of the degradation groove according to the preset degradation treatment temperature interval;

adjusting the real-time temperature of the hot air pipe according to the real-time temperature of the hot air pipe and the temperature interval of the hot air pipe, and determining that the real-time temperature of the hot air pipe is in the temperature interval of the hot air pipe;

adjusting the real-time temperature of the degradation tank according to the real-time temperature of the degradation tank and the temperature interval of the degradation tank, and determining that the real-time temperature of the degradation tank is in the temperature interval of the degradation tank;

and acquiring the adjusted real-time temperature of the hot air pipe and the adjusted real-time temperature of the degradation tank.

3. The method according to any one of claims 1 or 2, wherein the biochemical degradation apparatus further comprises a fan, and the adjusting the real-time temperature of the hot air duct according to the real-time temperature of the hot air duct and the temperature interval of the hot air duct to determine that the real-time temperature of the hot air duct is within the temperature interval of the hot air duct comprises:

determining that the real-time temperature of the hot air pipe is higher than the upper limit temperature of the hot air pipe temperature interval according to the real-time temperature of the hot air pipe and the hot air pipe temperature interval;

and reducing the air output of the fan, and reducing the temperature of the hot air pipe in real time to the temperature range of the hot air pipe within a first time threshold.

4. The method according to any one of claims 1 or 2, wherein the biochemical degradation apparatus further comprises a fan, and the adjusting the real-time temperature of the hot air duct according to the real-time temperature of the hot air duct and the temperature interval of the hot air duct to determine that the real-time temperature of the hot air duct is within the temperature interval of the hot air duct comprises:

determining that the real-time temperature of the hot air pipe is lower than the lower limit temperature of the hot air pipe temperature interval according to the real-time temperature of the hot air pipe and the hot air pipe temperature interval;

and increasing the air output of the fan, and increasing the real-time temperature of the hot air pipe to the temperature range of the hot air pipe within a second time threshold.

5. The method according to any one of claims 1 or 2, wherein the biochemical degradation apparatus further comprises at least one heating rod, and the adjusting the degradation tank real-time temperature according to the degradation tank real-time temperature and the degradation tank temperature interval and the determining that the degradation tank real-time temperature is within the degradation tank temperature interval comprise:

determining that the real-time temperature of the degradation tank is higher than the upper limit temperature of the temperature interval of the degradation tank according to the real-time temperature of the degradation tank and the temperature interval of the degradation tank;

and reducing the temperature of the at least one heating rod, and reducing the real-time temperature of the degradation tank to the temperature interval of the degradation tank within a third time threshold.

6. The method according to any one of claims 1 or 2, wherein the biochemical degradation apparatus further comprises at least one heating rod, and the adjusting the degradation tank real-time temperature according to the degradation tank real-time temperature and the degradation tank temperature interval and the determining that the degradation tank real-time temperature is within the degradation tank temperature interval comprise:

determining that the real-time temperature of the degradation tank is lower than the lower limit temperature of the temperature interval of the degradation tank according to the real-time temperature of the degradation tank and the temperature interval of the degradation tank;

and increasing the temperature of the at least one heating rod, and increasing the real-time temperature of the degradation tank within a fourth time threshold value to be within the temperature interval of the degradation tank.

7. The method according to any one of claims 1 to 6, wherein the biochemical degradation apparatus further comprises a touch display screen, and the temperature control operation is performed to adjust the temperature of the internal space of the biochemical degradation apparatus to be in the degradation process temperature range according to a preset degradation process temperature range, and the method further comprises:

adjusting the real-time temperature of the hot air pipe and/or the real-time temperature of the degradation tank;

determining that the real-time temperature of the degradation tank is not in the degradation tank temperature interval within a certain time threshold, and/or the real-time temperature of the hot air pipe is not in the hot air temperature interval;

and sending early warning to managers, and suspending the biochemical degradation treatment of the garbage.

8. A temperature control device is characterized by being applied to biochemical degradation equipment, wherein the biochemical degradation equipment comprises a hot air pipe and a degradation groove; the temperature control device comprises a processing unit and a communication unit, wherein,

9. A biochemical degradation device comprising a processor, a memory, a communication interface, and one or more programs stored in the memory and configured to be executed by the processor, the programs comprising instructions for performing the steps in the method of any of claims 1-8.

10. A computer-readable storage medium, characterized in that a computer program for electronic data exchange is stored, wherein the computer program causes a computer to perform the method according to any one of claims 1-8.