CN211847720U - A heat exchanger for aerobic fermentation tank of livestock and poultry manure - Google Patents
A heat exchanger for aerobic fermentation tank of livestock and poultry manure Download PDFInfo
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- CN211847720U CN211847720U CN202020226241.9U CN202020226241U CN211847720U CN 211847720 U CN211847720 U CN 211847720U CN 202020226241 U CN202020226241 U CN 202020226241U CN 211847720 U CN211847720 U CN 211847720U
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- 210000003608 fece Anatomy 0.000 title claims abstract description 18
- 244000144972 livestock Species 0.000 title claims abstract description 18
- 239000010871 livestock manure Substances 0.000 title claims abstract description 18
- 244000144977 poultry Species 0.000 title claims abstract description 18
- 238000010564 aerobic fermentation Methods 0.000 title claims abstract description 17
- 238000005192 partition Methods 0.000 claims abstract description 14
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical group [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims description 7
- 229910052782 aluminium Inorganic materials 0.000 claims description 7
- 239000000463 material Substances 0.000 claims 1
- 238000000855 fermentation Methods 0.000 abstract description 15
- 230000004151 fermentation Effects 0.000 abstract description 15
- 239000007789 gas Substances 0.000 abstract description 14
- 239000002699 waste material Substances 0.000 abstract description 4
- 239000002912 waste gas Substances 0.000 abstract description 3
- 230000000007 visual effect Effects 0.000 abstract 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000002918 waste heat Substances 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- 102000004190 Enzymes Human genes 0.000 description 1
- 108090000790 Enzymes Proteins 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000004332 deodorization Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A40/00—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
- Y02A40/10—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
- Y02A40/20—Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
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- Treatment Of Sludge (AREA)
- Fertilizers (AREA)
Abstract
Description
技术领域technical field
本实用新型属于农业机械技术领域,具体涉及一种畜禽粪便好氧发酵罐用热交换机。The utility model belongs to the technical field of agricultural machinery, in particular to a heat exchanger for an aerobic fermentation tank of livestock and poultry manure.
背景技术Background technique
畜禽粪便好氧发酵属于生物发酵,是国家大力推广一种应用技术,是生产有机肥料的一种较好的方法。在发酵过程中,为了让酵素组合高温菌繁殖发酵,需向畜禽粪便发酵罐通入适当温度的氧气。整个发酵罐设备能耗成本约占总生产成本的20%左右,因此节能减排任务较重。目前,国内许多企业发酵罐在发酵培养基灭菌、发酵过程产生的余热及发酵动力室(涡轮风泵、电机、液压机构等)产生的热量均没有得到有效的回收利用,造成能源资源的极大浪费。The aerobic fermentation of livestock and poultry manure belongs to biological fermentation. In the fermentation process, in order to allow the enzymes combined with high temperature bacteria to reproduce and ferment, oxygen at a suitable temperature needs to be introduced into the livestock and poultry manure fermentation tank. The energy consumption cost of the entire fermentation tank equipment accounts for about 20% of the total production cost, so the task of energy saving and emission reduction is relatively heavy. At present, the sterilization of fermentation medium, the waste heat generated by the fermentation process, and the heat generated by the fermentation power room (turbine air pump, motor, hydraulic mechanism, etc.) have not been effectively recycled in the fermentation tanks of many domestic enterprises, resulting in extreme energy resources. Big waste.
实用新型内容Utility model content
针对现有技术的不足,本实用新型提供一种畜禽粪便好氧发酵罐用热交换机,可以充分利用发酵罐发酵过程中产生的余热及动力室产生的热量,变废为宝,节约能源。Aiming at the deficiencies of the prior art, the utility model provides a heat exchanger for an aerobic fermentation tank of livestock and poultry manure, which can make full use of the waste heat generated in the fermentation process of the fermentation tank and the heat generated by the power room, turn waste into treasure and save energy.
本实用新型是通过以下技术方案实现的:The utility model is achieved through the following technical solutions:
一种畜禽粪便好氧发酵罐用热交换机,包括主壳、上盖、隔板和下壳,其中,所述隔板分别焊接于所述主壳的顶端及底端,所述上盖设置于所述主壳的顶端,所述下壳设置于所述主壳的底端;A heat exchanger for an aerobic fermentation tank of livestock and poultry manure, comprising a main shell, an upper cover, a partition plate and a lower shell, wherein the partition plate is welded to the top and bottom ends of the main shell respectively, and the upper cover is provided with at the top end of the main shell, the lower shell is arranged at the bottom end of the main shell;
所述上盖为圆台状,其顶端焊接有废气输出管道;The upper cover is in the shape of a truncated cone, the top of which is welded with an exhaust gas output pipe;
所述主壳为圆柱状,其顶端及底端的隔板之间焊接有一个以上的换热管;The main shell is cylindrical, and more than one heat exchange tube is welded between the top and bottom baffles;
所述下壳为圆柱状,其底部设置有4个小立柱用于支撑,其上端内凹成漏斗状,内部中空;The lower shell is cylindrical, the bottom of which is provided with 4 small uprights for support, the upper end of which is concave into a funnel shape, and the interior is hollow;
以主壳为主体视角,分为前后左右四个方向,所述主壳的侧面前部下方焊接有罐动力室气体接入管道,所述主壳的侧面后部上方焊接有接入动力室供风机管道;所述下壳的侧面右部上方焊接有罐顶热气体接入管道。Taking the main shell as the main perspective, it is divided into four directions: front, rear, left and right. The tank power room gas inlet pipe is welded under the side front of the main shell, and the power room supply pipe is welded above the side rear of the main shell. Fan pipeline; a tank top hot gas access pipeline is welded above the right part of the side surface of the lower shell.
优选地,所述主壳与所述上盖之间、所述主壳与所述下壳之间均通过法兰固定连接。Preferably, the main casing and the upper cover and between the main casing and the lower casing are all fixedly connected by flanges.
优选地,所述法兰上设置有20个均匀分布的直径为14mm的孔。Preferably, the flange is provided with 20 evenly distributed holes with a diameter of 14 mm.
优选地,所述隔板上设置有121个直径为38mm的贯穿孔,每纵排孔呈线性阵列,每两排之间的孔错位排列,所述换热管的数量为121根,与所述贯穿孔对应。Preferably, 121 through holes with a diameter of 38 mm are provided on the partition, each longitudinal row of holes is in a linear array, the holes between every two rows are arranged in a staggered arrangement, and the number of the heat exchange tubes is 121, which is the same as that of all the heat exchange tubes. The through hole corresponds to.
优选地,所述换热管的材质为铝,内部中空,管体中间大而两端小,管体被铝制外螺纹管包裹其中,管的两端可分别插入所述隔板上的贯穿孔内,并与所述隔板焊接于一体。Preferably, the heat exchange tube is made of aluminum, the interior is hollow, the tube body is large in the middle and the ends are small at both ends, the tube body is wrapped by an aluminum external threaded tube, and the two ends of the tube can be inserted into the through holes on the partition plate respectively. inside the hole and welded with the baffle.
本实用新型的有益效果如下:The beneficial effects of the present utility model are as follows:
与现有技术相比,本实用新型的畜禽粪便好氧发酵罐用热交换机充分利用发酵后产生的废气热量为继续发酵提供热量,变废为宝,节约能源;热交换机工作原理简单,结构合理,操作简单,制造成本低,安装快捷,维修方便,利于推广应用。Compared with the prior art, the heat exchanger for the aerobic fermentation tank of livestock and poultry manure of the present invention makes full use of the heat of waste gas generated after fermentation to provide heat for continued fermentation, turns waste into treasure, and saves energy; the heat exchanger has a simple working principle and a structure. Reasonable, simple in operation, low in manufacturing cost, quick in installation, convenient in maintenance, and beneficial for popularization and application.
附图说明Description of drawings
图1为畜禽粪便好氧发酵罐用热交换机的主视图;Fig. 1 is the front view of the heat exchanger used for the aerobic fermentation tank of livestock and poultry manure;
图2为畜禽粪便好氧发酵罐用热交换机的左视图;Fig. 2 is the left side view of the heat exchanger for the aerobic fermentation tank of livestock and poultry manure;
图3为畜禽粪便好氧发酵罐用热交换机移除上盖后的俯视图;Fig. 3 is the top view of the aerobic fermentation tank of livestock and poultry manure after removing the upper cover with the heat exchanger;
图中:1、废气输出管道;2、上盖;3、主壳;4、隔板;5、罐顶热气体接入管道;6、下壳;7、换热管;8、罐动力室气体接入管道;9、接入动力室供风机管道;10、贯穿孔。In the figure: 1. Exhaust gas output pipe; 2. Upper cover; 3. Main shell; Gas access pipeline; 9. Access to power room supply fan pipeline; 10. Through hole.
具体实施方式Detailed ways
下面结合附图与具体实施例对本实用新型做进一步详细说明。The present utility model will be further described in detail below with reference to the accompanying drawings and specific embodiments.
实施例1Example 1
一种畜禽粪便好氧发酵罐用热交换机,如图1所示,包括主壳3、上盖2、隔板4和下壳6,其中,所述隔板4分别焊接于所述主壳3的顶端及底端,所述上盖2设置于所述主壳3的顶端,所述下壳6设置于所述主壳3的底端。A heat exchanger for aerobic fermentation tank of livestock and poultry manure, as shown in Figure 1, includes a
所述上盖2为圆台状,其下部焊接有法兰,其顶端焊接有一直径250mm短管,用于连接废气输出管道1。The
所述主壳3为圆柱状,其顶端及底端均有法兰焊接于壳体上。The
所述下壳6为圆柱状,其上部焊接有法兰,其底部设置有4个小立柱用于支撑,其上端内凹成漏斗状,内部中空。The
所述主壳3与所述上盖2之间、所述主壳3与所述下壳6之间均添加密封圈并通过其各自的法兰用螺栓连接。所述法兰上均设置有20个均匀分布的直径为14mm的孔。Sealing rings are added between the
如图2所示,所述主壳3的顶端及底端的隔板4之间焊接有121根换热管7;如图3所示,隔板4上设置有121个直径为38mm的贯穿孔10,每纵排孔呈线性阵列,每两排之间的孔错位排列,所述换热管7与所述贯穿孔10对应。As shown in FIG. 2 , 121
所述换热管7的材质为铝,内部中空,管体中间大而两端小,管体被铝制外螺纹管包裹其中,管的两端可分别插入所述隔板4上的贯穿孔10内,并与所述隔板4焊接于一体。The
如图1所示,以主壳3为主体视角,分为前后左右四个方向。所述主壳3的侧壁前部下方焊接有一直径250mm短管,用于连接罐动力室气体接入管道8;所述主壳3的侧壁后部上方焊接有一直径160mm短管,用于连接接入动力室供风机管道9;所述下壳6的侧壁右部上方焊接有一直径250mm短管,用于连接罐顶热气体接入管道5。As shown in FIG. 1 , with the
一种畜禽粪便好氧发酵罐用热交换机的运行工艺,具体如下:发酵罐中发酵产生的热废气通过罐顶热气体接入管道5进入换热管7,换热管7将热废气中热量吸收,之后废气通过废气输出管道1排出,进入后续的喷淋除臭装置中;从罐动力室吸进的气体通过罐动力室气体接入管道8进入热交换机主壳3内,将换热管7上的热量带走,并进入接入动力室供风机管道9用于后续发酵所需热氧气用。An operation process of a heat exchanger for an aerobic fermentation tank of livestock and poultry manure is as follows. The heat is absorbed, and then the exhaust gas is discharged through the exhaust
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CN111153716A (en) * | 2020-02-28 | 2020-05-15 | 盐城工业职业技术学院 | A heat exchanger for aerobic fermentation tank of livestock and poultry manure and its operation process |
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Assignee: Qianxiao Wanqi (Yancheng) Technology Co.,Ltd. Assignor: YANCHENG INSTITUTE OF INDUSTRY TECHNOLOGY Contract record no.: X2023980047353 Denomination of utility model: A heat exchanger for aerobic fermentation tanks of livestock and poultry manure Granted publication date: 20201103 License type: Common License Record date: 20231118 |
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