CN110793007A - Reheating steam combined middle-exhaust steam heating water supply and heat supply system and method - Google Patents
Reheating steam combined middle-exhaust steam heating water supply and heat supply system and method Download PDFInfo
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
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- F22B1/00—Methods of steam generation characterised by form of heating method
- F22B1/02—Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers
- F22B1/08—Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers the heat carrier being steam
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
- F01K7/00—Steam engine plants characterised by the use of specific types of engine; Plants or engines characterised by their use of special steam systems, cycles or processes; Control means specially adapted for such systems, cycles or processes; Use of withdrawn or exhaust steam for feed-water heating
- F01K7/34—Steam engine plants characterised by the use of specific types of engine; Plants or engines characterised by their use of special steam systems, cycles or processes; Control means specially adapted for such systems, cycles or processes; Use of withdrawn or exhaust steam for feed-water heating the engines being of extraction or non-condensing type; Use of steam for feed-water heating
- F01K7/38—Steam engine plants characterised by the use of specific types of engine; Plants or engines characterised by their use of special steam systems, cycles or processes; Control means specially adapted for such systems, cycles or processes; Use of withdrawn or exhaust steam for feed-water heating the engines being of extraction or non-condensing type; Use of steam for feed-water heating the engines being of turbine type
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
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- F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
- F01K7/00—Steam engine plants characterised by the use of specific types of engine; Plants or engines characterised by their use of special steam systems, cycles or processes; Control means specially adapted for such systems, cycles or processes; Use of withdrawn or exhaust steam for feed-water heating
- F01K7/34—Steam engine plants characterised by the use of specific types of engine; Plants or engines characterised by their use of special steam systems, cycles or processes; Control means specially adapted for such systems, cycles or processes; Use of withdrawn or exhaust steam for feed-water heating the engines being of extraction or non-condensing type; Use of steam for feed-water heating
- F01K7/40—Use of two or more feed-water heaters in series
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22G—SUPERHEATING OF STEAM
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Abstract
本发明提供了一种再热蒸汽联合中排蒸汽加热给水供热系统,包括纯凝汽轮火力发电机组和组合式供热系统;纯凝汽轮火力发电机组主要包括锅炉、汽轮机高压缸、汽轮机中压缸、汽轮机低压缸、高压加热器、除氧器、低压加热器、凝汽器、给水前置泵、汽动给水泵;组合式供热系统主要包括一级表面式给水加热器、蒸汽发生器、二级表面式蒸汽加热器。本发明提供了一种再热蒸汽联合中排蒸汽加热给水供热方法。本发明利用了中排蒸汽的过热度,机组排汽量更小,冷端损失更小,机组效率更高,能级梯度利用更为合理;利用蒸发器代替直接喷水换热,供热参数更稳定,波动小。系统结构合理,系统可靠,负荷适应性好,主机安全性高。
The invention provides a reheat steam combined middle-exhaust steam heating water supply heating system, including a pure condensing turbine thermal power generating unit and a combined heating system; the pure condensing turbine thermal power generating unit mainly includes a boiler, a steam turbine high-pressure cylinder, a steam turbine Medium pressure cylinder, steam turbine low pressure cylinder, high pressure heater, deaerator, low pressure heater, condenser, feedwater prepump, steam-driven feedwater pump; the combined heating system mainly includes a first-level surface feedwater heater, steam Generator, secondary surface steam heater. The invention provides a method for heating feed water with reheat steam combined with middle-row steam heating. The invention utilizes the superheat degree of the middle-exhaust steam, the steam exhaust volume of the unit is smaller, the cold end loss is smaller, the unit efficiency is higher, and the energy level gradient utilization is more reasonable; More stable and less volatile. The system structure is reasonable, the system is reliable, the load adaptability is good, and the host safety is high.
Description
技术领域technical field
本发明属于能源技术领域,尤其涉及一种用于新型节能的蒸汽联合给水供热系统及方法。The invention belongs to the technical field of energy, and in particular relates to a new energy-saving steam combined water supply heating system and method.
背景技术Background technique
为了提高机组经济性、响应国家节能减排的号召,目前,国内大部分火电机组都进行了技术改造,对外进行抽汽供热。In order to improve the economy of the unit and respond to the national call for energy conservation and emission reduction, at present, most domestic thermal power units have undergone technological transformation, and they are extracting steam for heat supply to the outside world.
火电机组进行抽汽供热改造,经济性的提高幅度与抽汽参数、抽汽量、抽汽位置等多个因素有关。在相同供热需求的前提下,选择适合机组的具有最大经济性的抽汽方案是研究热力系统的重点。The improvement of the economical efficiency of thermal power units is related to many factors such as extraction parameters, extraction volume, extraction location and so on. Under the premise of the same heating demand, choosing the most economical steam extraction scheme suitable for the unit is the focus of research on thermal systems.
目前,常规的供热方式为选定若干抽汽源,根据参数要求采用直接喷水节流方式进行减温减压,对外进行供热。这种供热方式存在如下缺陷:机组排汽量大,冷端损失大,机组效率低,能级梯度利用不合理;喷水换热的供热参数不稳定,波动大。At present, the conventional heating method is to select a number of steam extraction sources, and use the direct water spray throttling method to reduce temperature and pressure according to the parameter requirements, and supply heat to the outside. This heating method has the following defects: large exhaust steam volume of the unit, large cold end loss, low unit efficiency, and unreasonable utilization of energy level gradient; the heating parameters of water spray heat exchange are unstable and fluctuate greatly.
发明内容SUMMARY OF THE INVENTION
本发明要解决的技术问题是提供一种结构合理,系统可靠,负荷适应性好,供热参数波动小,主机安全性高的抽汽供热系统。The technical problem to be solved by the present invention is to provide a steam extraction heating system with reasonable structure, reliable system, good load adaptability, small fluctuation of heating parameters and high safety of the main engine.
为了解决上述技术问题,本发明的技术方案是提供一种再热蒸汽联合中排蒸汽加热给水供热系统,其特征在于:包括纯凝汽轮火力发电机组和组合式供热系统;In order to solve the above-mentioned technical problems, the technical scheme of the present invention is to provide a reheat steam combined middle-exhaust steam heating water supply heating system, which is characterized in that: it includes a pure condensing turbine thermal power generating unit and a combined heating system;
所述纯凝汽轮火力发电机组包括锅炉,锅炉蒸汽出口连接汽轮机高压缸进口,汽轮机高压缸出口连接锅炉再热蒸汽进口,锅炉再热蒸汽出口连接汽轮机中压缸进口,汽轮机中压缸出口连接汽轮机低压缸进口,汽轮机低压缸出口连接凝汽器进口,凝汽器出口连接低压加热器一侧进口,低压加热器该侧出口连接除氧器进口,除氧器出口连接高压加热器一侧进口,高压加热器该侧出口连接锅炉蒸汽进口;The pure condensing turbine thermal power generating unit comprises a boiler, the steam outlet of the boiler is connected to the inlet of the high-pressure cylinder of the steam turbine, the outlet of the high-pressure cylinder of the steam turbine is connected to the inlet of the reheated steam of the boiler, the outlet of the reheated steam of the boiler is connected to the inlet of the middle-pressure cylinder of the steam turbine, and the outlet of the middle-pressure cylinder of the steam turbine is connected to the inlet of the steam turbine. The inlet of the low-pressure cylinder of the steam turbine, the outlet of the low-pressure cylinder of the steam turbine is connected to the inlet of the condenser, the outlet of the condenser is connected to the inlet of the low-pressure heater, the outlet of the low-pressure heater is connected to the inlet of the deaerator, and the outlet of the deaerator is connected to the inlet of the high-pressure heater , the outlet of this side of the high-pressure heater is connected to the steam inlet of the boiler;
所述组合式供热系统包括一级表面式给水加热器,一级表面式给水加热器低温侧进口连接所述除氧器出口,一级表面式给水加热器低温侧出口连接蒸汽发生器进口,一级表面式给水加热器高温侧进口连接所述汽轮机中压缸出口,一级表面式给水加热器高温侧出口连接除氧器进口;蒸汽发生器出口连接二级表面式饱和蒸汽加热器低温侧进口,二级表面式饱和蒸汽加热器高温侧进口连接所述汽轮机高压缸出口和/或所述汽轮机中压缸进口,二级表面式饱和蒸汽加热器高温侧出口连接蒸汽发生器进口,二级表面式饱和蒸汽加热器低温侧出口连接对外供热管路。The combined heating system comprises a primary surface feedwater heater, the low temperature side inlet of the primary surface feedwater heater is connected to the outlet of the deaerator, and the low temperature side outlet of the primary surface feedwater heater is connected to the steam generator inlet, The high temperature side inlet of the primary surface feedwater heater is connected to the outlet of the medium pressure cylinder of the steam turbine, the high temperature side outlet of the primary surface feedwater heater is connected to the deaerator inlet; the steam generator outlet is connected to the low temperature side of the secondary surface saturated steam heater Inlet, the high temperature side inlet of the secondary surface saturated steam heater is connected to the outlet of the high pressure cylinder of the steam turbine and/or the inlet of the middle pressure cylinder of the steam turbine, the high temperature side outlet of the secondary surface saturated steam heater is connected to the inlet of the steam generator, and the secondary surface saturated steam heater is connected to the inlet of the steam generator. The low temperature side outlet of the surface saturated steam heater is connected to the external heating pipeline.
优选地,所述除氧器出口连接给水前置泵进口,给水前置泵出口连接汽动给水泵进口,汽动给水泵出口连接所述高压加热器一侧进口。Preferably, the outlet of the deaerator is connected to the inlet of the feedwater prepump, the outlet of the feedwater prepump is connected to the inlet of the steam-powered feed pump, and the outlet of the steam-powered feed pump is connected to the inlet on one side of the high-pressure heater.
更优选地,所述一级表面式给水加热器低温侧进口连接所述给水前置泵出口。More preferably, the low temperature side inlet of the first-stage surface feedwater heater is connected to the outlet of the feedwater prepump.
优选地,所述一级表面式给水加热器利用所述汽轮机中压缸出口的中排蒸汽,对所述除氧器出口的部分给水进行一次加热;所述中排蒸汽降温后引至所述除氧器。Preferably, the first-stage surface feedwater heater uses the middle row steam at the outlet of the middle pressure cylinder of the steam turbine to heat part of the feedwater at the outlet of the deaerator once; the middle row steam is cooled and then led to the Deaerator.
更优选地,所述蒸汽发生器利用经所述二级表面式蒸汽加热器换热后的再热蒸汽,对所述一级表面式给水加热器出口的给水进行混合式二次加热,将其蒸发为饱和蒸汽。More preferably, the steam generator uses the reheated steam after heat exchange by the secondary surface type steam heater to perform mixed secondary heating on the feedwater at the outlet of the primary surface type feedwater heater, and heat it. Evaporates to saturated steam.
进一步地,所述二级表面式蒸汽加热器利用所述汽轮机高压缸出口和/或所述中压缸入口的再热蒸汽,对所述蒸汽发生器出口的饱和蒸汽进行三次加热;经过所述二级表面式蒸汽加热器加热后的过热蒸汽对外供热。Further, the secondary surface type steam heater uses the reheated steam at the outlet of the high-pressure cylinder of the steam turbine and/or the inlet of the medium-pressure cylinder to heat the saturated steam at the outlet of the steam generator three times; The superheated steam heated by the secondary surface steam heater supplies external heat.
本发明还提供了一种再热蒸汽联合中排蒸汽加热给水供热方法,其特征在于:采用上述的再热蒸汽联合中排蒸汽加热给水供热系统,包括如下步骤:The present invention also provides a method for heating feed water with reheated steam combined with middle-row steam, which is characterized in that: adopting the above-mentioned reheated steam combined with middle-row steam to heat the water supply heating system, comprising the following steps:
步骤1:低压给水被中排蒸汽一次表面式加热;Step 1: The low-pressure feed water is surface-heated once by the middle-row steam;
所述低压给水由除氧器出口引出,低压给水首先经过一级表面式给水加热器进行一次表面式加热,加热热源为汽轮机中压缸出口的中排蒸汽;The low-pressure feed water is drawn from the outlet of the deaerator, and the low-pressure feed water is first surface-heated by a first-stage surface feed water heater, and the heating heat source is the middle-exhaust steam at the outlet of the middle-pressure cylinder of the steam turbine;
步骤2:低压给水被再热蒸汽二次混合加热;Step 2: The low pressure feed water is mixed and heated by the reheated steam for a second time;
经过步骤1加热后的低压给水进入蒸汽发生器,蒸汽发生器的加热热源为经过二级表面式饱和蒸汽加热器换热后的再热蒸汽;在蒸汽发生器中,经过步骤1加热后的低压给水被所述再热蒸汽混合加热,并蒸发为饱和蒸汽;The low-pressure feed water heated in step 1 enters the steam generator, and the heating source of the steam generator is the reheated steam after heat exchange by the secondary surface saturated steam heater; in the steam generator, the low-pressure feed water heated in step 1 The feed water is mixed and heated by the reheated steam and evaporated into saturated steam;
步骤3:饱和蒸汽被再热蒸汽三次表面式加热;Step 3: Saturated steam is surface-heated three times by reheated steam;
步骤2产生的饱和蒸汽进入二级表面式饱和蒸汽加热器,被加热至过热蒸汽对外供热;二级表面式饱和蒸汽加热器的加热热源为汽轮机高压缸出口和/或汽轮机中压缸入口的再热蒸汽。The saturated steam generated in
与传统的抽汽直接减温减压供热系统相比,本发明提供的再热蒸汽联合中排蒸汽加热给水供热系统具有如下有益效果:Compared with the traditional steam extraction and direct desuperheating and decompression heating system, the reheat steam combined middle-exhaust steam heating water supply heating system provided by the present invention has the following beneficial effects:
1、利用了中排蒸汽的过热度,机组排汽量更小,冷端损失更小,机组效率更高,能级梯度利用更为合理;1. Using the superheat degree of the middle exhaust steam, the exhaust steam volume of the unit is smaller, the cold end loss is smaller, the unit efficiency is higher, and the energy level gradient utilization is more reasonable;
2、利用蒸发器代替直接喷水换热,供热参数更稳定,波动小。2. Using the evaporator to replace the direct water spray heat exchange, the heating parameters are more stable and the fluctuation is small.
3、结构合理,系统可靠,负荷适应性好,主机安全性高。3. Reasonable structure, reliable system, good load adaptability and high host safety.
附图说明Description of drawings
图1为本实施例提供的再热蒸汽联合中排蒸汽加热给水供热系统示意图;1 is a schematic diagram of a reheat steam combined middle-row steam heating feed water heating system provided by the present embodiment;
附图标记说明:Description of reference numbers:
1—锅炉,2—汽轮机高压缸,3—汽轮机中压缸,4—汽轮机低压缸,5—高压加热器,6—除氧器,7—低压加热器,8—凝汽器,9—给水前置泵,10—汽动给水泵,11—一级表面式给水加热器,12—蒸汽发生器,13—二级表面式饱和蒸汽加热器。1—boiler, 2—turbine high pressure cylinder, 3—steam turbine medium pressure cylinder, 4—steam turbine low pressure cylinder, 5—high pressure heater, 6—deaerator, 7—low pressure heater, 8—condenser, 9—feed water Front pump, 10—steam-driven feed water pump, 11—first-level surface feedwater heater, 12—steam generator, 13—secondary surface-type saturated steam heater.
具体实施方式Detailed ways
下面结合具体实施例,进一步阐述本发明。The present invention will be further described below in conjunction with specific embodiments.
图1为本实施例提供的再热蒸汽联合中排蒸汽加热给水供热系统示意图,所述的再热蒸汽联合中排蒸汽加热给水供热系统包括锅炉1、汽轮机高压缸2、汽轮机中压缸3、汽轮机低压缸4、高压加热器5、除氧器6、低压加热器7、凝汽器8、给水前置泵9、汽动给水泵10、一级表面式给水加热器11、蒸汽发生器12、二级表面式饱和蒸汽加热器13等。1 is a schematic diagram of the reheat steam combined middle row steam heating feed water heating system provided by the present embodiment, the reheat steam combined middle row steam heating feed water heating system includes a boiler 1, a steam turbine
其中,锅炉1、汽轮机高压缸2、汽轮机中压缸3、汽轮机低压缸4、高压加热器5、除氧器6、低压加热器7、凝汽器8、给水前置泵9、汽动给水泵10共同构成常规的纯凝汽轮火力发电机组。Among them, boiler 1, steam turbine
一级表面式给水加热器11、蒸汽发生器12、二级表面式饱和蒸汽加热器13共同构成组合式供热系统。组合式供热系统利用纯凝汽轮火力发电机组的中排蒸汽、再热蒸汽将低压给水加热至过热蒸汽,对外供热。The primary surface type feed water heater 11, the
具体结构如下:The specific structure is as follows:
纯凝汽轮火力发电机组包括锅炉1,锅炉1蒸汽出口连接汽轮机高压缸2进口,汽轮机高压缸2出口连接锅炉1再热蒸汽进口,锅炉1再热蒸汽出口连接汽轮机中压缸3进口,汽轮机中压缸3出口连接汽轮机低压缸4进口,汽轮机低压缸4出口连接凝汽器8进口,凝汽器8出口连接低压加热器7一侧进口,低压加热器7该侧出口连接除氧器6进口,除氧器6出口连接给水前置泵9进口,给水前置泵9出口连接汽动给水泵10进口,汽动给水泵10出口连接高压加热器5一侧进口,高压加热器5该侧出口连接锅炉1蒸汽进口。The pure condensing turbine thermal power generating set includes boiler 1, the steam outlet of boiler 1 is connected to the inlet of
组合式供热系统包括一级表面式给水加热器11,一级表面式给水加热器11低温侧进口连接给水前置泵9出口,一级表面式给水加热器11低温侧出口连接蒸汽发生器12进口,一级表面式给水加热器11高温侧进口连接汽轮机中压缸3出口,一级表面式给水加热器11高温侧出口连接除氧器6进口。蒸汽发生器12出口连接二级表面式饱和蒸汽加热器13低温侧进口,二级表面式饱和蒸汽加热器13高温侧进口连接汽轮机高压缸2出口和/或汽轮机中压缸3进口,二级表面式饱和蒸汽加热器13高温侧出口连接蒸汽发生器12进口,二级表面式饱和蒸汽加热器13低温侧出口连接对外供热管路。The combined heating system includes a primary surface feedwater heater 11, the low temperature side inlet of the primary surface feedwater heater 11 is connected to the outlet of the feedwater prepump 9, and the low temperature side outlet of the primary surface feedwater heater 11 is connected to the
本实施例中,一级表面式给水加热器11的被加热工质取自除氧器6出口的低压给水,加热后引至蒸汽发生器12,加热工质取自汽轮机中压缸3出口的中排蒸汽,换热后引至除氧器6。In this embodiment, the heated working fluid of the first-stage surface feedwater heater 11 is taken from the low-pressure feedwater at the outlet of the
二级表面式饱和蒸汽加热器13的被加热工质来自蒸汽发生器12出口的饱和蒸汽,饱和蒸汽被加热至过热对外供热,加热工质取自汽轮机高压缸2出口的或汽轮机中压缸3进口的再热蒸汽,换热后引至蒸汽发生器12。The heated working fluid of the secondary surface
蒸汽发生器12的被加热工质来自一级表面式给水加热器11出口的低压给水,加热工质取自二级表面式饱和蒸汽加热器13出口的再热蒸汽,低压给水在蒸汽发生器12内与再热蒸汽混合加热为饱和蒸汽后引至二级表面式饱和蒸汽加热器13。The heated working fluid of the
本实施例提供的再热蒸汽联合中排蒸汽加热给水供热系统的工作过程如下:The working process of the reheat steam combined middle-exhaust steam heating water supply heating system provided by this embodiment is as follows:
工作过程的被加热介质为低压给水,加热介质为中排蒸汽和再热蒸汽。工作过程主要分为三个流程。The heated medium in the working process is low-pressure feed water, and the heating medium is the middle row steam and the reheated steam. The work process is mainly divided into three processes.
第一流程,低压给水被中排蒸汽一次表面式加热。该系统的低压给水由给水前置泵9出口母管引出,低压给水首先经过一级表面式给水加热器11进行一次表面式加热。加热热源为汽轮机中压缸3出口的中排蒸汽。In the first process, the low-pressure feed water is surface-heated by the middle-exhaust steam. The low-pressure feedwater of the system is drawn from the outlet main pipe of the feedwater prepump 9, and the low-pressure feedwater first passes through the primary surface feedwater heater 11 for primary surface heating. The heating heat source is the middle exhaust steam from the outlet of the
第二流程,低压给水被再热蒸汽二次混合加热。经过第一流程加热后的低压给水进入蒸汽发生器12,该流程热源为经过第三流程换热后的再热蒸汽。在蒸汽发生器12中,低压给水被再热蒸汽混合加热,蒸发为饱和蒸汽。In the second process, the low-pressure feed water is mixed and heated by the reheated steam. The low-pressure feed water heated by the first process enters the
第三流程,饱和蒸汽被再热蒸汽三次表面式加热。第二流程产生的饱和蒸汽进入二级表面式饱和蒸汽加热器13,被加热至过热蒸汽对外供热。加热热源为汽轮机高压缸2出口或汽轮机中压缸3入口的再热蒸汽。In the third process, the saturated steam is surface-heated three times by the reheated steam. The saturated steam generated in the second process enters the secondary surface saturated
本发明提供的再热蒸汽联合中排蒸汽加热给水供热系统先利用中排蒸汽的过热度加热给水再进入蒸汽发生器,蒸汽发生器的蒸发热源采用再热蒸汽,再热蒸汽的过热度首先用于蒸汽器出口饱和蒸汽的过热吸热,然后再进入蒸发器,提供饱和水转变至饱和蒸汽所需的潜热。与抽汽直接减温减压供热系统相比,本系统利用了中排蒸汽的过热度,机组排汽量更小,冷端损失更小,机组效率更高,能级梯度利用更为合理。The reheat steam combined middle row steam heating feed water heating system provided by the present invention first uses the superheat degree of the middle row steam to heat the feed water and then enters the steam generator. The evaporation heat source of the steam generator adopts reheat steam, and the superheat degree of the reheat steam is first It is used for superheat absorption of saturated steam at the steamer outlet, and then enters the evaporator to provide the latent heat required for the conversion of saturated water to saturated steam. Compared with the direct desuperheating and decompression heating system of extraction steam, this system utilizes the superheat degree of the middle exhaust steam, the exhaust steam volume of the unit is smaller, the cold end loss is smaller, the unit efficiency is higher, and the utilization of energy level gradient is more reasonable. .
与抽汽直接减温减压供热系统相比,本系统利用蒸发器代替直接喷水换热,供热参数更稳定,波动小。以600MW的汽轮发电机组对外供热400t/h为例,应用本系统后,机组发电煤耗下降4.5g/kWh,全年发电量按330000万kWh,每年节煤量为14850t,标煤单价按800元/t,全年增加毛收益约1188万元。Compared with the direct desuperheating and decompression heating system with steam extraction, this system uses the evaporator to replace the direct water spray heat exchange, and the heating parameters are more stable and the fluctuation is small. Taking the 600MW steam turbine generator set as an example to supply 400t/h of external heat, after the application of this system, the coal consumption of the unit for power generation is reduced by 4.5g/kWh, the annual power generation is 3300 million kWh, the annual coal saving is 14850t, and the unit price of standard coal is based on 800 yuan / t, the annual increase in gross income is about 11.88 million yuan.
以上所述,仅为本发明的较佳实施例,并非对本发明任何形式上和实质上的限制,应当指出,对于本技术领域的普通技术人员,在不脱离本发明方法的前提下,还将可以做出若干改进和补充,这些改进和补充也应视为本发明的保护范围。凡熟悉本专业的技术人员,在不脱离本发明的精神和范围的情况下,当可利用以上所揭示的技术内容而做出的些许更动、修饰与演变的等同变化,均为本发明的等效实施例;同时,凡依据本发明的实质技术对上述实施例所作的任何等同变化的更动、修饰与演变,均仍属于本发明的技术方案的范围内。The above are only preferred embodiments of the present invention, and are not intended to limit the present invention in any form or substance. It should be pointed out that for those skilled in the art, without departing from the method of the present invention, the Several improvements and supplements can be made, and these improvements and supplements should also be regarded as the protection scope of the present invention. All those skilled in the art, without departing from the spirit and scope of the present invention, can utilize the above-disclosed technical content to make some changes, modifications and equivalent changes of evolution, all belong to the present invention. Equivalent embodiments; at the same time, any modification, modification and evolution of any equivalent changes made to the above embodiments according to the essential technology of the present invention still fall within the scope of the technical solutions of the present invention.
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