CN116036741A - Tea making waste gas recycling device - Google Patents
Tea making waste gas recycling device Download PDFInfo
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- CN116036741A CN116036741A CN202310203356.4A CN202310203356A CN116036741A CN 116036741 A CN116036741 A CN 116036741A CN 202310203356 A CN202310203356 A CN 202310203356A CN 116036741 A CN116036741 A CN 116036741A
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- 239000002912 waste gas Substances 0.000 title claims abstract description 34
- 238000004064 recycling Methods 0.000 title claims abstract description 16
- 239000007789 gas Substances 0.000 claims abstract description 121
- 241001122767 Theaceae Species 0.000 claims abstract description 30
- 238000010438 heat treatment Methods 0.000 claims abstract description 27
- 238000000034 method Methods 0.000 claims abstract description 22
- 230000008569 process Effects 0.000 claims abstract description 20
- 238000011084 recovery Methods 0.000 claims description 59
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 24
- 238000003860 storage Methods 0.000 claims description 14
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims description 9
- 239000010949 copper Substances 0.000 claims description 9
- 229910052802 copper Inorganic materials 0.000 claims description 9
- 239000004744 fabric Substances 0.000 claims description 9
- 239000011941 photocatalyst Substances 0.000 claims description 6
- 230000001105 regulatory effect Effects 0.000 claims description 6
- 239000000463 material Substances 0.000 claims description 4
- 229920000742 Cotton Polymers 0.000 claims description 3
- 230000005540 biological transmission Effects 0.000 claims description 3
- 230000007246 mechanism Effects 0.000 claims description 3
- SOQBVABWOPYFQZ-UHFFFAOYSA-N oxygen(2-);titanium(4+) Chemical group [O-2].[O-2].[Ti+4] SOQBVABWOPYFQZ-UHFFFAOYSA-N 0.000 claims description 3
- 230000009467 reduction Effects 0.000 abstract description 11
- 238000012545 processing Methods 0.000 abstract description 8
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- 238000004134 energy conservation Methods 0.000 abstract 1
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- 238000004659 sterilization and disinfection Methods 0.000 description 1
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28B—STEAM OR VAPOUR CONDENSERS
- F28B1/00—Condensers in which the steam or vapour is separate from the cooling medium by walls, e.g. surface condenser
- F28B1/06—Condensers in which the steam or vapour is separate from the cooling medium by walls, e.g. surface condenser using air or other gas as the cooling medium
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/0027—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with additional separating or treating functions
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/0027—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with additional separating or treating functions
- B01D46/0028—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with additional separating or treating functions provided with antibacterial or antifungal means
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/0027—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with additional separating or treating functions
- B01D46/0038—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with additional separating or treating functions with means for influencing the odor, e.g. deodorizing substances
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/10—Particle separators, e.g. dust precipitators, using filter plates, sheets or pads having plane surfaces
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/86—Catalytic processes
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28B—STEAM OR VAPOUR CONDENSERS
- F28B9/00—Auxiliary systems, arrangements, or devices
- F28B9/02—Auxiliary systems, arrangements, or devices for feeding steam or vapour to condensers
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28B—STEAM OR VAPOUR CONDENSERS
- F28B9/00—Auxiliary systems, arrangements, or devices
- F28B9/08—Auxiliary systems, arrangements, or devices for collecting and removing condensate
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Abstract
Description
技术领域technical field
本发明涉及废气回收利用的技术领域,特别是涉及一种制茶废气回收利用装置。The invention relates to the technical field of waste gas recovery and utilization, in particular to a tea making waste gas recovery and utilization device.
背景技术Background technique
茶叶加工设备的正常使用离不开能源的供给,茶叶加工设备所需的能源主要分为传统化石能源和清洁能源两种类型,其中清洁能源主要有电力、液化石油气、天然气、微波、远红外以及生物质燃料等。目前,在热能燃料趋于清洁化和节能化的发展趋势下,利用锯末、森林枝条、稻草以及麦秆等加工而成的生物质颗粒燃料受到业界的重视,由于它们的生产成本较低,其在茶叶加工方面开始被越来越多地应用。The normal use of tea processing equipment is inseparable from the supply of energy. The energy required by tea processing equipment is mainly divided into two types: traditional fossil energy and clean energy. Among them, clean energy mainly includes electricity, liquefied petroleum gas, natural gas, microwave, and far-infrared energy. and biomass fuels. At present, under the development trend of thermal fuels tending to be clean and energy-saving, biomass pellet fuels processed from sawdust, forest branches, rice straw, and wheat straw are valued by the industry. Due to their low production costs, their It has been used more and more in tea processing.
然而,在茶叶的加工生产过程中,茶叶加工设备整体的热能利用率较低,其中的大部分热量都以制茶产生的废气(热气及水蒸汽)形式流失,造成了极大的能源浪费,茶叶加工过程中所产生的气体及水蒸气等能源具有很高的回收利用价值。近年来,为了实现“节能减排、降低能耗”的发展理念,研制一种对制茶废气进行回收与二次循环利用的设备是当下迫切需要解决的一个问题。However, in the process of tea processing and production, the overall heat utilization rate of tea processing equipment is low, and most of the heat is lost in the form of waste gas (hot air and water vapor) generated from tea making, resulting in a huge waste of energy. Energy such as gas and water vapor generated during tea processing has high recycling value. In recent years, in order to realize the development concept of "energy saving, emission reduction, and energy consumption reduction", it is an urgent problem to develop a device for recycling and secondary recycling of tea-making waste gas.
发明内容Contents of the invention
本发明的目的是提供一种制茶废气回收利用装置,以解决上述现有技术存在的问题,使制茶过车中产生的废气能够进行回收并再利用,实现节能减排、降低能耗的目的。The purpose of the present invention is to provide a tea-making waste gas recovery and utilization device to solve the above-mentioned problems in the prior art, so that the waste gas generated in the tea-making process can be recycled and reused, so as to realize energy saving, emission reduction and energy consumption reduction. Purpose.
为实现上述目的,本发明提供了如下方案:To achieve the above object, the present invention provides the following scheme:
本发明提供了一种制茶废气回收利用装置,包括机架、第一集气装置、第二集气装置、加热装置、第一气体回收装置和第二气体回收装置,所述机架上设置有相互连通的所述第一集气装置和第二集气装置,所述第一集气装置用于将制茶过程中产生的废气排至所述第二集气装置内,所述第二集气装置内设置有所述加热装置和所述第一气体回收装置,所述第二集气装置通过所述第一气体回收装置与所述第二集气装置连通,所述第一气体回收装置或者所述第二气体回收装置用于与供热系统连通。The invention provides a tea-making waste gas recovery and utilization device, which includes a frame, a first gas collection device, a second gas collection device, a heating device, a first gas recovery device and a second gas recovery device. There are the first gas collecting device and the second gas collecting device communicated with each other, the first gas collecting device is used to discharge the waste gas generated in the tea making process into the second gas collecting device, the second gas collecting device The heating device and the first gas recovery device are arranged in the gas collection device, the second gas collection device communicates with the second gas collection device through the first gas recovery device, and the first gas recovery device The device or the second gas recovery device is used to communicate with the heating system.
优选的,所述第一集气装置包括抽风机和电机,所述电机通过带轮传动机构与所述抽风机连接,所述抽风机的进风口与制茶过程中产生的废气源连通、出风口与所述第二集气装置连通。Preferably, the first gas collecting device includes an exhaust fan and a motor, the motor is connected to the exhaust fan through a pulley transmission mechanism, the air inlet of the exhaust fan communicates with the waste gas source generated in the tea making process, and the outlet The tuyere is in communication with the second gas collecting device.
优选的,所述抽风机的出风口上设置有过滤网,所述过滤网为光触媒布网,所述光触媒布网的材质为纳米二氧化钛负载棉织物。Preferably, the air outlet of the exhaust fan is provided with a filter net, the filter net is a photocatalyst cloth net, and the material of the photocatalyst cloth net is cotton fabric loaded with nano-titanium dioxide.
优选的,所述抽风机为离心式风机,输出转速为2400r/min,流量为12662-17343m3/h,全压为3100-2740Pa,电机功率为18.5-2kw。Preferably, the exhaust fan is a centrifugal fan with an output speed of 2400r/min, a flow rate of 12662-17343m3/h, a total pressure of 3100-2740Pa, and a motor power of 18.5-2kw.
优选的,所述第二集气装置为一密闭箱体,所述第二集气装置的底部设置有所述第一气体回收装置和冷凝水回收装置、侧壁上设置有所述加热装置。Preferably, the second gas collection device is a closed box, the bottom of the second gas collection device is provided with the first gas recovery device and the condensed water recovery device, and the heating device is provided on the side wall.
优选的,所述加热装置包括至少两个单管式热交换器,所述单管式热交换器包括翅片和椭圆铜管,所述翅片等间距设置,所述椭圆铜管螺旋贯穿所述翅片中。Preferably, the heating device includes at least two single-tube heat exchangers, the single-tube heat exchanger includes fins and elliptical copper tubes, the fins are arranged at equal intervals, and the elliptical copper tubes spiral through the in the fins.
优选的,所述冷凝水回收装置包括过滤嘴、调节阀和出水管,所述过滤嘴设置于所述第二集气装置的底板下方,所述过滤嘴通过所述调节阀与所述出水管连通,所述出水管连接冷凝水收集装置。Preferably, the condensed water recovery device includes a filter, a regulating valve and an outlet pipe, the filter is arranged under the bottom plate of the second gas collecting device, and the filter is communicated with the outlet pipe through the regulating valve, so that The water outlet pipe is connected to the condensed water collection device.
优选的,所述第一气体回收装置包括负压风机和气泵,所述第二集气装置的下方设置有一底仓,所述底仓的上面设置有若干个所述负压风机,所述气泵设置于所述底仓的底板下方且与所述底仓连通,所述气泵通过导气管与所述第二气体回收装置的储气罐连通。Preferably, the first gas recovery device includes a negative pressure fan and an air pump, a bottom chamber is arranged below the second gas collecting device, and several negative pressure fans are arranged above the bottom chamber, and the air pump The air pump is arranged under the bottom plate of the bottom chamber and communicated with the bottom chamber, and the air pump communicates with the air storage tank of the second gas recovery device through an air guide pipe.
优选的,所述气泵通过导气管与制茶工艺系统的供热源连通。Preferably, the air pump communicates with the heat supply source of the tea-making process system through an air duct.
优选的,所述第二气体回收装置包括储气罐和空气压缩机,所述空气压缩机的一端与所述第二集气装置的一侧连通、另一端通过导气管与所述储气罐连通。Preferably, the second gas recovery device includes an air storage tank and an air compressor, one end of the air compressor communicates with one side of the second gas collection device, and the other end communicates with the air storage tank through an air duct connected.
本发明相对于现有技术取得了以下技术效果:Compared with the prior art, the present invention has achieved the following technical effects:
本发明的制茶废气回收利用装置,通过将制茶所产生的废气进行二次回收并再次利用,解决了茶叶加工工艺系统中能源回收利用方面所出现的能源浪费问题,可为企业实现降本增效,达到节能减排、降低能耗的目的。The tea-making waste gas recovery and utilization device of the present invention solves the problem of energy waste in the energy recovery and utilization of the tea processing system by secondary recycling and reuse of the waste gas generated in tea production, and can reduce costs for enterprises Increase efficiency to achieve energy saving, emission reduction and energy consumption reduction.
附图说明Description of drawings
为了更清楚地说明本发明实施例或现有技术中的技术方案,下面将对实施例中所需要使用的附图作简单地介绍,显而易见地,下面描述中的附图仅仅是本发明的一些实施例,对于本领域普通技术人员来讲,在不付出创造性劳动的前提下,还可以根据这些附图获得其他的附图。In order to more clearly illustrate the technical solutions in the embodiments of the present invention or the prior art, the following will briefly introduce the accompanying drawings required in the embodiments. Obviously, the accompanying drawings in the following description are only some of the present invention. Embodiments, for those of ordinary skill in the art, other drawings can also be obtained based on these drawings without any creative effort.
图1为本发明制茶废气回收利用装置的结构示意图;Fig. 1 is the structural representation of the waste gas recycling device for tea making of the present invention;
图2为本发明中第一集气装置的结构示意图;Fig. 2 is the structural representation of the first gas collecting device among the present invention;
图3为本发明中第二集气装置的内部结构示意图;Fig. 3 is a schematic diagram of the internal structure of the second gas collecting device in the present invention;
图4为本发明中气体回收装置的结构示意图;Fig. 4 is the structural representation of gas recovery device among the present invention;
图5为本发明中第一气体回收装置的结构示意图二;Fig. 5 is the structural schematic diagram II of the first gas recovery device in the present invention;
图6为本发明中加热装置的结构示意图;Fig. 6 is the structural representation of heating device among the present invention;
图7为本发明中冷凝水回收装置的结构示意图;Fig. 7 is the structural representation of the condensed water recovery device in the present invention;
其中:1-机架;2-第一集气装置,20-电机,21-抽风机,22-过滤网;3-第二集气装置,30-过滤嘴,31-调节阀,32-出水管;4-加热装置,41-单管式热交换器,42-椭圆铜管,43-翅片;5-第一气体回收装置,51-负压风机,52-导气管,53-气泵;6-第二气体回收装置,61-储气罐,62-空气压缩机。Among them: 1-frame; 2-first gas collection device, 20-motor, 21-exhauster fan, 22-filter; 3-second gas collection device, 30-filter, 31-regulating valve, 32-outlet pipe ;4-heating device, 41-single tube heat exchanger, 42-elliptical copper tube, 43-fin; 5-first gas recovery device, 51-negative pressure fan, 52-air duct, 53-air pump; 6 -Second gas recovery device, 61 -air storage tank, 62 -air compressor.
具体实施方式Detailed ways
下面将结合本发明实施例中的附图,对本发明实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例仅仅是本发明一部分实施例,而不是全部的实施例。基于本发明中的实施例,本领域普通技术人员在没有付出创造性劳动的前提下所获得的所有其他实施例,都属于本发明保护的范围。The following will clearly and completely describe the technical solutions in the embodiments of the present invention with reference to the accompanying drawings in the embodiments of the present invention. Obviously, the described embodiments are only some, not all, embodiments of the present invention. Based on the embodiments of the present invention, all other embodiments obtained by persons of ordinary skill in the art without making creative efforts belong to the protection scope of the present invention.
本发明的目的是提供一种制茶废气回收利用装置,以解决现有技术存在的问题,使制茶过车中产生的废气能够进行回收并再利用,实现节能减排、降低能耗的目的。The purpose of the present invention is to provide a tea-making waste gas recovery and utilization device to solve the problems existing in the prior art, so that the waste gas generated in the tea-making process can be recycled and reused, so as to achieve the purpose of energy saving, emission reduction and energy consumption reduction .
为使本发明的上述目的、特征和优点能够更加明显易懂,下面结合附图和具体实施方式对本发明作进一步详细的说明。In order to make the above objects, features and advantages of the present invention more comprehensible, the present invention will be further described in detail below in conjunction with the accompanying drawings and specific embodiments.
如图1至图7所示:本实施例提供了一种制茶废气回收利用装置,包括机架1、第一集气装置2、第二集气装置3、加热装置4、第一气体回收装置5和第二气体回收装置6,机架1上设置有相互连通的第一集气装置2和第二集气装置3,第一集气装置2用于将制茶过程中产生的废气排至第二集气装置3内,第二集气装置3内设置有加热装置4和第一气体回收装置5,第二集气装置3通过第一气体回收装置5与第二集气装置3连通,第一气体回收装置5或者第二气体回收装置6用于与供热系统连通。As shown in Figures 1 to 7: this embodiment provides a tea making waste gas recovery and utilization device, including a
第一集气装置2包括抽风机21和电机20,电机20通过带轮传动机构与抽风机21连接,抽风机21的进风口与制茶过程中产生的废气源连通、出风口与第二集气装置3连通。抽风机21的出风口上设置有过滤网22,用于过滤掉制茶所产生的绒毛以及杂质,过滤网22为光触媒布网,光触媒布网的材质为纳米二氧化钛负载棉织物,此种过滤网22负载牢固、纳米尺度高、致密均匀、性能良好,在空气净化、异味消除、杀菌消毒、水质净化、除臭等领域效果显著;在光照射下产生的活性物质具备抗菌除臭、有机物去除、空气净化、油污分解、防霉等功能,能够更好的提升气体的过滤和除杂效果。抽风机21为离心式风机,输出转速为2400r/min,流量为12662-17343m3/h,全压为3100-2740Pa,电机20功率为18.5-2kw,该型号的抽风21机具有良好的气动性能、运转平衡、振动小、效率高、使用寿命长等特点。The first
第二集气装置3为一密闭箱体,第二集气装置3的底部设置有第一气体回收装置5和冷凝水回收装置、侧壁上设置有加热装置4,第二集气装置3内的废气及水蒸气进行二次辅助加热,形成过热饱和水蒸气以及高温热风。加热装置4包括至少两个单管式热交换器41,单管式热交换器41包括翅片43和椭圆铜管42,翅片43等间距设置,椭圆铜管42螺旋贯穿翅片43中,外形尺寸为150×230cm;翅片43和椭圆铜管42的材质优选用导热系数相对较高的紫铜,以便更好的导出热量完成整个热量的传递过程。冷凝水回收装置包括过滤嘴30、调节阀31和出水管32,过滤嘴30设置于第二集气装置3的底板下方,过滤嘴30通过调节阀31与出水管32连通,出水管32连接冷凝水收集装置。水蒸气冷凝过程所散发的热量可达蒸汽全热量的20%-30%,且压力、温度越高,冷凝过程具有的热量就越多,占蒸汽总热量的比例也就越大,高温蒸汽携带的热量相当于同等质量水所携带热量的5-6倍,利用水蒸汽的潜热,可提高设备的加热效率;如果能够100%的回收冷凝过程的热量,并加以有效利用,则锅炉所需要的燃料可节约20%-30%。本实施例通过综合利用高压蒸汽冷凝过程所产生的余热,可以节约高达25%左右的热能。The second
第一气体回收装置包括负压风机51和气泵53,第二集气装置3的下方设置有一底仓,底仓的上面设置有若干个负压风机51,气泵53设置于底仓的底板下方且与底仓连通,气泵53通过导气管52与第二气体回收装置6的储气罐61连通。本实施例中安装有6个型号、大小相同的负压风机51,负压风机51的进风口与第二集气装置3的上仓连通、出风口与底仓连通,其风量为3300m3/h,转速为1400r/min,用于将第二集气装置3内经过辅助加热后形成过热饱和水蒸气以及高温热风吸入至底仓内;气泵53型号为PCV-2M/2MSV,气泵电机的功率为125w,额定工作电压为230V,抽气速率为50L/min,重量约为3.2kg,气泵53用于将底仓内的气体通过导气管52导入至储气罐61内。气泵53通过导气管52与制茶工艺系统的供热源连通。第二气体回收装置6包括储气罐61和空气压缩机62,空气压缩机62的一端与第二集气装置3的一侧连通、另一端通过导气管52与储气罐61连通,空气压缩机62优选型号为7.5SFb,排气量为1.12m3/min,排气压力为0.8MPa,额定工作电压为380V,额定功率为7.5kw,外形尺寸为980mm×650mm×880mm,总重量为80kg;该型号的空气压缩机62排气量大、工作稳定性强、适用范围广,故障率低。其中,制茶废气经二次处理后成为高压蒸汽,储气罐61是用来储存这些高压蒸汽的,储气罐61中的高温、高压蒸汽可输送至储气井或是导入至单个的气瓶中,用于各种制造行业的需求;经二次加热后的蒸汽中含有较高的潜热,回收利用二次蒸汽往往可以节约10%左右的能源,可以用它进行低温换热,第二气体回收装置6中的高温气体可以直接用于制茶工艺系统、洗浴用水、供热系统或者其他低温工艺,储气罐61内的高温高压气体也可用于高温切割、激光切割、重型卡车制造业和各种高温高压喷气设备等等。The first gas recovery device includes a
本实施例通过综合利用制茶废气中蒸汽冷凝和气体所产生的余热,经过二次加热处理,可有效回收利用其中热量,并合理排放冷凝水和储存高温高压气体,提高设备加热效率和生产效率,降低能耗和节约能源。In this embodiment, through the comprehensive utilization of the waste heat generated by steam condensation and gas in the tea-making waste gas, after secondary heating treatment, the heat can be effectively recovered and utilized, and the condensed water can be discharged reasonably and the high-temperature and high-pressure gas can be stored to improve the heating efficiency and production efficiency of the equipment. , Reduce energy consumption and save energy.
本说明书中应用了具体个例对本发明的原理及实施方式进行了阐述,以上实施例的说明只是用于帮助理解本发明的方法及其核心思想;同时,对于本领域的一般技术人员,依据本发明的思想,在具体实施方式及应用范围上均会有改变之处。综上所述,本说明书内容不应理解为对本发明的限制。In this description, specific examples are used to illustrate the principle and implementation of the present invention. The description of the above embodiments is only used to help understand the method and core idea of the present invention; meanwhile, for those of ordinary skill in the art, according to this The idea of the invention will have changes in the specific implementation and scope of application. In summary, the contents of this specification should not be construed as limiting the present invention.
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CN109730167A (en) * | 2019-01-30 | 2019-05-10 | 日照盛华茶业机械股份有限公司 | Tea drum fixation machine energy conservation device for improving quality |
CN216363502U (en) * | 2021-12-06 | 2022-04-26 | 宜昌同飞机械设备有限公司 | Heat recovery device of tea leaf fixation machine |
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