九、發明說明： 【發明所屬之技術領域】 且特別是有關於一 之連續生質能碳化 種 系 本發明是有關於一種碳化系統， 可快速將非粉狀碳材原料進行碳化 統。 【先前技術】 "傳統的生質能碳化設備，是在—Μ的碳化窯内以批 么式的方式進行，批次式的碳化程序首先將塊狀生質能推 r炭化窯。再藉由間接加熱或部份自燃:，以將生質能溫度 提高到碳化溫度後’再將碳化窯所有的入σ封死以斷絕氧 軋進入，當碳化窯内的溫度低於約攝氏5(rc後，便可開窯 取出生質能碳。 … 雖然傳統的生質能碳化方法可達到預期的使用目 的’但是該批次式生質能碳化缺點是： 1. 碳化週期長（7天〜30天）。 2. 人工進料與人工出料，故人力需求高相對提高製 造成本。 .人工燒寞，碳化製程中溫度不均，故碳料品質不一 致’使得收碳率較低。 上述二者’以碳化週期長影響生質能碳製造成本為最 為了加速產里通常是在同一地區設置數十個批次式的 反化黨’來達到可以連續產出生質能碳的目的。惟此多碳 化窯策略卻有系統複雜、人力需求更高，以及生質能碳品 質不一的缺點β 【發明内容】 種連續式生質能碳 工進料、取料進而 因此，本發明之目的就是在提供一 化系統，用以解決傳統碳化設備利用人 &南人力需求的缺點。 曰的就更在提供 个货明之另 ,.,,m 從堤續式生質能碳 化糸、冼，用以解決傳統碳化設備 诘许，1©太曰I 刀而求阿，導致生產 迷度k、產$少的缺點。 化目的就是在提供一種連續式生質能碳 化糸統，用以解決傳統碳化設備之碳化過程因加熱空氣含 有過咼含氧量而引發自燃現象之缺點。 ,、 =發明之又-目的就是在提供―種連續式生質能碳 =系統，用以解決傳統碳化設備之高溫溫度不均一，提高 石及材之損耗，故造成碳材品質不一的缺點。 根據本發明之上述目的，提供一種連續式生質能碳化 系統，包含-提供—碳化之高溫尾氣的生質能氣化爐以及 -生質能碳化爐。該生質能碳化爐具有一碳化爐本體、形 成於該碳化爐本體上且供連續送入多數碳材原料的一進 料口、—供導入該生質能氣化爐產出之高溫尾氣的熱源輸 入编、一供輸出高溫尾氣的熱源輸出端、一冷卻端，以及 一供排放生質能碳料的出料口，該碳化爐本體具有一鄰近 於該熱源輸入端的碳化區、一與該碳化區相連通且鄰近該 進料口的乾燥區，以及一與該碳化區相連通且鄰近該冷卻 尾氣導入該生質能碳化爐中，所以可在短時間内快速提升 碳化作用的所需的高溫’故可大幅提升生產速度，而且產 S多。 3.藉由生質能氣化爐持續將含氡量低的高溫尾氣導入 該生質能碳化爐中，故可避免碳化過程中出現自燃現象。 4_利用該生質能氣化爐持續供應攝氏13〇(rc左右的 高溫，故在碳化製程中可提高高溫之均溫性，且大幅提升 碳材的含碳量，以及有效提高碳材之品質。 【實施方式】 參照第1圖，係繪示本發明的一實施例之連續式生質 能碳化系統。 參照第4圖，係繪示該實施例的流程圖。 參照第1圖與第4圖。該連續式生質能碳化系統包含 一生質能氣化爐100、一生質能碳化爐200、一冷卻單元 300，以及一自動出料單元4〇〇。 參照第2圖，係繪示本發明之該生質能氣化皞1〇〇與 高壓送風機140之詳細結構圖。 參照第1圖與第2圖。該生質能氣化爐i 〇〇具有一氣 化爐體110、一内藏式（embedded)燃燒管12〇、一氣化空氣 官130，以及一高壓送風機14〇β生質能燃料是從上方的 一生質能進料口 111進入圓柱型的氣化爐内。位於底部的 排灰栅欄116支撐著整個反應爐。在燃燒過程中，生質能 燃料藉重力依序通過乾燥區112、熱裂解區113及還原區 1321204 114，最後的餘炭（char)則在爐底的燃燒區115中與空氣充 分混合，直到餘炭（char)完全燃燒成灰後掉入底層的儲灰 桶 117。 該生質能氣化爐100是藉由高壓送風機14〇抽風，經 由氣化空氣管130在爐床的上面沿著柱狀面分散地向中心 強迫送入氣化空氣提供燃燒區115餘碳燃燒所需之空氣。 而該生質能氣化爐100内燃燒管122所需的燃燒空氣也是 由高壓送風機140通入燃燒空氣，與來自爐内之氣化燃氣 混合並完全燃燒後排出。在還原區114與熱裂解區113所 產生的合成燃氣經由内藏式燃燒管120下半壁的複數孔隙 121進入此内藏式燃燒管120中。該内藏式燃燒管12〇不 僅是提供合成燃氣經由排氣管123排出氣化爐的通道，也 是合成氣化燃氣的燃燒室。合成氣化燃氣在内藏式燃燒管 120中與外部引入的二次燃燒空氣混合並完全燃燒成高溫 而且潔淨的排氣，而此排氣的主要成份為二氧化碳 與水（H2〇)與氮（A)，過剩氧可以控制在很低的程度，排 氣中不含焦油與飛灰。 本發明的生質能氣化爐100,採以生質能燃料向下移 動而氣化合成氣體逆流向上的燃燒方式，生質能燃燒在乾 燥區112被乾燥，在缺氧高溫的熱裂解區113被熱裂解， 以產生熱裂解燃氣與餘炭（char)，乾燥與熱裂解所需要的 熱能主要是由爐床燃燒區115燃燒餘炭的排氣所提供，燃 燒區115的輻射熱也有部份的貢獻。在還原區114中，二 氧化碳（c〇2)與水（H2〇)被餘炭藉多布爾（B〇und〇urard)反應 9 尾氣101給該生質能碳化爐200，以及將碳材原料201持 續投入該碳化爐本體210内部。此時，該生質能氣化爐i 〇〇 所產生之尚溫尾氣1〇1(溫度高達攝氏1300°C左右，且不含 氧氣〇2)導入該生質能碳化爐200之碳化區2 11的下緣， 使得碳化區211内的碳材得以在短時間内快速提升至碳化 作用所需的高溫（該碳化區211可達到高溫攝氏3〇〇。〇〜9〇〇 °C)’而此時乾燥區212的溫度為攝氏60°C〜250°C。 快速冷卻，並取出生質能碳料： 接著，經碳化區211之高溫碳化的生質能碳料202逐 漸落入冷卻區213時，該冷卻單元300(本實施例申是—泵 浦）亦同時自冷卻端250泵入低於攝氏150°C的冷卻流體 310，在本實施例中，該冷卻流體310可為氮（n2)、二氧化 碳（C〇2)或水蒸氣（H2〇)。因此，從碳化區211下降來的高 溫生質能碳快速冷卻到攝氏150°C以下（該冷卻區213的溫 度為攝氏150°C〜500°C ) ’便可連續取出生質能碳料202。 自動出料： 生質能碳料202由該出料口 260產出時，該自動出料 單元400藉由一馬達410之控制，並利用一輸送帶42〇(及 履帶）將生質能碳料202輸送至一儲料槽（圖未揭示）内，以 達到自動化定時定量出料的目的。 更進一步地，本發明連續式生質能碳化系統更包含一 自動進料單元（圖未揭示）。該自動進料單元是由定量器與 台車升降輸送單元所組成。藉由定量器將定量的生質能碳 材原料201裝入台車’再藉升降輸送執道將台車内的生質 1321204 能碳材原料201投入生質能碳化爐本體2J0的進料口 2別/一達到自動化供料的目的。在此並呼應於上述自動出 料早^使本發明之連續式生質能碳化系統在供料與出料 上，均能達到自動化連續生產，使生質能碳料2〇2品質一 致，以及節省人力成本之各項優點。 歸納上述’相較於傳統人工黨燒生質能碳料之系統複 雜、碳化週期長、高人力需求以及生質能碳料品質不一的 缺點，本發明之連續式生質能碳化系統確實可達到以下功 效與優點： 1·藉由該生質能氣化爐100及自動進料單元分別經熱 源輸入端230、進料口 220持續供應碳化之高溫尾氣1〇1 及碳材原料201至該生質能碳化爐2〇〇 ’使該生質能碳化 爐200得以在短時間内快速提升碳化作用所需的溫度。再 藉由β亥自動出料單元4〇〇定時定量地快速輸送生質能碳料 202，使得本發明之連續式生質能碳化系統達到大幅縮減 碳化週期，進而獲致快速量產生質能碳料202、生質能碳 料202品質一致’以及減少人力需求，相對可大幅降低人 力成本與製造成本的優點。 2.藉由冷卻單元300提供不含氧氣的低溫冷卻流體 3 10 ’將由碳化區211降下的生質能碳料202快速冷卻至攝 氏150 C以下’在攝氏150°C以下生質能碳料202不會因 接觸空氣中的氧而發生自燃’所以，可連續排料至儲料 槽’由空氣自然冷卻降溫。因此，本發明利用供應低含氧 量之高溫尾氣101 ’避免碳化過程中出現自燃現象，降低 12 1321204 碳材在碳化過程中的損耗，故可有效提高碳材之產能。 3. 相較於傳統碳化設備之溫度不均導致碳化品質不一 致的缺點。本發明之連續式生質能碳化系統以連續式供應 碳化之高溫尾氣 '碳材的方式，可提高碳化製程的高溫均 ’性，以大幅提升碳材的含碳量，相對提高生質能碳料的 品質。 4. 相較於傳統碳化設備因加熱空氣含有過高含氧量而 引發自燃現象。本發明利用供應低含氧量之高溫尾氣 101，可避免碳化過程中出現自燃現象，以降低碳材在碳 化過程中的損耗，故取碳率極高，並有效提高碳材之產能。 參照第1圖，此外，更值得一提的是，經由本發明之該 生質能碳化爐200的熱源輸出端24〇所產生的熱能，可提供 作為能源回收再利用的作用，如此，使本發明之連續式生質 能碳化系統亦具有連續產出回收用熱源的功用，針對地球上 有限資源越來越短缺的情況下，本發明更兼具有製造能源再 利用的功效與優點。 —雖然本發明已以一實施例揭露如上，然其並非用以限 林發明，任何熟習此技藝者，在*麟本發明之精神和 範圍内’當可作錢之更動與潤飾，因此本發明之保護範 圍當視後附之申請專利範圍所界定者為準。 【圖式簡單說明】 為讓本發明之上述和其他目的、特徵 能更明顯易懂，所附圖式之詳細說明如下：、Ά施例 13 U212U4 第1圖是繪示本發明一實施例的連續式生質能碳化系 統的設備组合之流程圖。 第2圖是繪示該實施例之生質能氣化爐詳細結構圖。 第3圖是繪示該實施例之生質能碳化爐的局部放大 圖。 第4圖是繪示該實施例的流程圖。IX. INSTRUCTIONS: [Technical field to which the invention pertains] and in particular to a continuous biomass carbonization species The present invention relates to a carbonization system for rapidly carbonizing a non-powdered carbon material. [Prior Art] "The traditional biomass carbonization equipment is carried out in a batch-type manner in a carbonization kiln of Μ, and the batch-type carbonization process first pushes the bulk biomass to the carbonization kiln. Indirect heating or partial auto-ignition: to increase the temperature of the biomass to the carbonization temperature, and then seal all the σ of the carbonization kiln to cut off the oxygen rolling, when the temperature in the carbonization kiln is lower than about 5 degrees Celsius. (After rc, the kiln can be used to remove the biomass carbon. ... Although the traditional biomass carbonization method can achieve the intended purpose of use', the disadvantages of this batch type biomass carbonization are: 1. Long carbonization cycle (7 days) ~30 days) 2. Manual feeding and manual discharging, so the manpower demand is high and the manufacturing cost is increased. The artificial burning, the temperature in the carbonization process is uneven, so the carbon material quality is inconsistent, which makes the carbon collection rate lower. Both of them 'the long-term carbonization cycle affects the cost of biomass energy carbon production is the most accelerated production. Usually, dozens of batch-type counter-revolutionaries are set up in the same area to achieve the goal of continuous production of biomass energy. However, the multi-carbon kiln strategy has the disadvantages of complicated system, higher manpower demand, and different quality of biomass carbon. [Inventive content] Continuous type of biomass energy carbon feed, reclaiming, and thus, the present invention The purpose is to provide one The system is used to solve the shortcomings of the traditional carbonization equipment to meet the needs of human & South manpower. The more it is to provide a cargo, the other, from the distillation of biomass energy, carbonization, bismuth, to solve the traditional The carbonization equipment promises that 1© too 曰I knife and seek for the shortcomings, resulting in the production of aggravation k, the production of less. The purpose is to provide a continuous biomass carbonization system to solve the carbonization of traditional carbonization equipment The process is caused by the fact that the heated air contains excessive oxygen content and causes spontaneous combustion phenomenon. , = The invention is again - the purpose is to provide a kind of continuous biomass energy carbon = system to solve the high temperature temperature unevenness of the traditional carbonization equipment. According to the above object of the present invention, a continuous biomass energy carbonization system comprising a biomass gasification furnace for providing a carbonized high-temperature exhaust gas and a catalyst is provided to improve the loss of stone and material. a biomass energy carbonization furnace having a carbonization furnace body, a feed port formed on the carbonization furnace body for continuously feeding a plurality of carbon material raw materials, and being introduced into the biomass gasification furnace output a heat source input of the high temperature exhaust gas, a heat source output end for outputting the high temperature exhaust gas, a cooling end, and a discharge port for discharging the biomass energy carbon material, the carbonization furnace body having a carbonization zone adjacent to the heat source input end a drying zone in communication with the carbonization zone adjacent to the feed port, and a communication with the carbonization zone and adjacent to the cooling tail gas into the biomass energy carbonization furnace, so that the carbonization can be rapidly increased in a short time. The required high temperature' can greatly increase the production speed and produce more S. 3. By introducing the high-temperature exhaust gas with low strontium content into the biomass energy carbonization furnace by the biomass gasifier, carbonization can be avoided. Self-ignition occurs in the process. 4_Using the biomass gasifier to continuously supply a high temperature of about 13 摄C (the temperature around rc is increased, so the temperature uniformity of the high temperature can be increased in the carbonization process, and the carbon content of the carbon material is greatly increased, And effectively improve the quality of carbon materials. [Embodiment] Referring to Fig. 1, there is shown a continuous mass-energy carbonization system according to an embodiment of the present invention. Referring to Figure 4, a flow chart of this embodiment is shown. Refer to Figures 1 and 4. The continuous biomass energy carbonization system comprises a biomass gasification furnace 100, a biomass energy carbonization furnace 200, a cooling unit 300, and an automatic discharge unit 4〇〇. Referring to Fig. 2, there is shown a detailed structural view of the biomass gasification 皞1〇〇 and the high pressure blower 140 of the present invention. Refer to Figures 1 and 2. The biomass gasifier i 〇〇 has a gasification furnace body 110, an embedded combustion tube 12〇, a gasification air officer 130, and a high pressure blower 14〇β biomass fuel from above The primary energy feed port 111 enters the cylindrical gasifier. A ash barrier 116 at the bottom supports the entire reactor. During the combustion process, the biomass energy fuel passes through the drying zone 112, the thermal cracking zone 113 and the reduction zone 1321204 114 by gravity, and the last char (char) is thoroughly mixed with the air in the combustion zone 115 of the furnace bottom until After the char is completely burned to ash, it falls into the ash storage tank 117 of the bottom layer. The biomass gasifier 100 is evacuated by a high-pressure blower 14 to provide a combustion zone 115 for combustion of carbon through a gasification air tube 130 on the upper surface of the hearth along the columnar surface to forcefully feed the gasification air toward the center. The air needed. The combustion air required for the combustion tube 122 in the biomass gasification furnace 100 is also introduced into the combustion air by the high-pressure blower 140, mixed with the gasification gas from the furnace, and completely burned and discharged. The synthetic gas produced in the reduction zone 114 and the thermal cracking zone 113 enters the built-in combustion tube 120 via a plurality of pores 121 in the lower half of the built-in combustion tube 120. The built-in combustion tube 12 is not only a passage for supplying synthetic gas to the gasification furnace via the exhaust pipe 123, but also a combustion chamber for synthesizing gasification gas. The synthetic gasification gas is mixed with the externally introduced secondary combustion air in the inner combustion tube 120 and completely burned into a high temperature and clean exhaust gas, and the main components of the exhaust gas are carbon dioxide and water (H2〇) and nitrogen. (A), excess oxygen can be controlled to a very low degree, and the exhaust gas contains no tar and fly ash. The biomass gasification furnace 100 of the present invention adopts a combustion mode in which the biomass fuel moves downward and the gasification synthesis gas flows countercurrently upward, and the biomass energy combustion is dried in the drying zone 112, in the thermal cracking zone of the anoxic high temperature. 113 is thermally cracked to produce pyrolysis gas and char (char). The heat energy required for drying and thermal cracking is mainly provided by the exhaust gas of the combustion charcoal in the combustion zone 115 of the hearth, and the radiant heat of the combustion zone 115 is also Contribution. In the reduction zone 114, the carbon dioxide (c〇2) and the water (H2〇) are reacted by the waste charcoal by a multi-bureau (B〇und〇urard) 9 exhaust gas 101 to the biomass energy carbonization furnace 200, and the carbon material raw material 201 The inside of the carbonization furnace body 210 is continuously supplied. At this time, the thermal exhaust gas 1〇1 (the temperature is up to about 1300 ° C and containing no oxygen enthalpy 2) generated by the biomass gasifier i 导入 is introduced into the carbonization zone 2 of the biomass energy carbonization furnace 2 The lower edge of 11 allows the carbon material in the carbonization zone 211 to be rapidly increased to a high temperature required for carbonization in a short time (the carbonization zone 211 can reach a high temperature of 3 摄 〇 〇〇 〇〇 〇〇 〇〇 〇〇 ) ) 而 而 而At this time, the temperature of the drying zone 212 is 60 ° C to 250 ° C. Rapid cooling and removal of the bio-energy carbon material: Next, when the high-temperature carbonized bioenergy carbon material 202 of the carbonization zone 211 gradually falls into the cooling zone 213, the cooling unit 300 (this embodiment is a pump) At the same time, the cooling fluid 250 is pumped into the cooling fluid 310 below 150 ° C. In the present embodiment, the cooling fluid 310 may be nitrogen (n2), carbon dioxide (C〇2) or water vapor (H2〇). Therefore, the high-temperature biomass carbon dropped from the carbonization zone 211 is rapidly cooled to below 150 ° C (the temperature of the cooling zone 213 is 150 ° C to 500 ° C) "can continuously remove the biomass energy carbon material 202 . Automatic Discharge: When the biomass energy carbon material 202 is produced by the discharge port 260, the automatic discharge unit 400 is controlled by a motor 410 and utilizes a conveyor belt 42 (and a crawler belt) to convert the biomass carbon. The material 202 is conveyed to a hopper (not shown) for automated timing and quantitative discharge. Furthermore, the continuous biomass energy carbonization system of the present invention further comprises an automatic feed unit (not shown). The automatic feeding unit is composed of a doser and a trolley lifting and conveying unit. The quantitative raw material carbon material raw material 201 is loaded into the trolley by the doser, and the raw material 1321204 of the biomass in the trolley can be put into the feed port 2 of the biomass energy carbonization furnace body 2J0. / One achieves the purpose of automated feeding. In this case, in response to the above automatic discharging, the continuous biomass energy carbonization system of the present invention can achieve automatic continuous production on the feeding and discharging, so that the quality of the raw material carbon material is uniform, and Save the advantages of labor costs. The above-mentioned continuous biomass energy carbonization system of the present invention can be summarized as a disadvantage of the above-mentioned complex system, the long carbonization cycle, the high manpower requirement and the quality of the biomass energy carbon material compared with the traditional artificial party burning biomass carbon material. The following functions and advantages are achieved: 1. The biomass gasification furnace 100 and the automatic feeding unit continuously supply the carbonized high-temperature exhaust gas 1〇1 and the carbon material raw material 201 through the heat source input end 230 and the feed port 220, respectively. The biomass carbonization furnace 2' enables the biomass calcination furnace 200 to rapidly increase the temperature required for carbonization in a short time. Then, the QGH automatic discharging unit 4 is used to rapidly and quantitatively transport the biomass energy carbon material 202, so that the continuous biomass energy carbonization system of the present invention can greatly reduce the carbonization cycle, thereby obtaining a rapid mass production of the mass energy carbon material. 202, the quality of the biomass energy carbon material 202 is consistent' and the manpower demand is reduced, which can greatly reduce the labor cost and the manufacturing cost. 2. Providing the oxygen-free cryogenic cooling fluid 3 10 ' by the cooling unit 300 to rapidly cool the biomass energy carbon material 202 lowered by the carbonization zone 211 to below 150 C C. The biomass energy carbon material 202 below 150 ° C. It does not spontaneously ignite due to exposure to oxygen in the air. Therefore, it can be continuously discharged to the storage tank', which is naturally cooled by air to cool down. Therefore, the present invention utilizes the high-temperature exhaust gas 101' which supplies low oxygen content to avoid spontaneous combustion in the carbonization process and reduce the loss of the carbon material in the carbonization process of 12 1321204, thereby effectively increasing the productivity of the carbon material. 3. The disadvantage of inconsistent carbonization quality compared to the temperature unevenness of conventional carbonization equipment. The continuous biomass energy carbonization system of the invention can continuously increase the high temperature uniformity of the carbonization process by continuously supplying the carbonized high-temperature exhaust gas 'carbon material, so as to greatly increase the carbon content of the carbon material and relatively increase the biomass carbon. The quality of the material. 4. Spontaneous combustion is caused by the excessive oxygen content of heated air compared to conventional carbonization equipment. The invention utilizes the high-temperature exhaust gas 101 which supplies low oxygen content, can avoid the spontaneous combustion phenomenon in the carbonization process, and reduces the loss of the carbon material in the carbonization process, so the carbon ratio is extremely high, and the productivity of the carbon material is effectively improved. Referring to Fig. 1, in addition, it is more worth mentioning that the heat energy generated by the heat source output terminal 24 of the biomass energy carbonization furnace 200 of the present invention can provide an effect of recycling as an energy source. The continuous biomass energy carbonization system of the invention also has the function of continuously generating a heat source for recycling, and in view of the increasing shortage of limited resources on the earth, the invention has the advantages and advantages of manufacturing energy reuse. </ RTI> Although the invention has been disclosed in an embodiment above, it is not intended to limit the invention, and any person skilled in the art will be able to make money changes and refinements within the spirit and scope of the invention. The scope of protection is subject to the definition of the scope of the patent application. BRIEF DESCRIPTION OF THE DRAWINGS In order to make the above and other objects and features of the present invention more apparent, the detailed description of the drawings is as follows: Example 13 U212U4 FIG. 1 is a diagram showing an embodiment of the present invention. Flowchart of a combination of equipment for a continuous biomass energy carbonization system. Fig. 2 is a detailed structural view showing the biomass gasifier of this embodiment. Fig. 3 is a partially enlarged view showing the biomass energy carbonization furnace of the embodiment. Figure 4 is a flow chart showing this embodiment.
【主要元件符號說明】 100:生質能氣化爐 1〇1 :高溫尾氣 110 :氣化爐體 111 :生質能進料口 112 :乾燥區 U3 :熱裂解區 114 :還原區 115 :燃燒區 116 :排灰柵攔 117 :儲灰桶 120:内藏式燃燒管 121 :孔隙 122 :燃燒管 123 :排氣管 130 :氣化空氣管 140 :高壓送風機 2〇〇 :生質能碳化爐 2 01 :碳材原料 202 :生質能碳料 21〇 :碳化爐本體 211 :碳化區 212 :乾燥區 213 :冷卻區 220 :進料口 230 :熱源輸入端 240 :熱源輸出端 250 :冷卻端 260 :出料口 1321204 300 :冷卻單元 310 :冷卻流體 400 :自動出料單元 410 :馬達 420 :輸送帶[Main component symbol description] 100: Biomass gasifier 1〇1: High temperature exhaust gas 110: Gasification furnace body 111: Biomass energy feed port 112: Drying zone U3: Thermal cracking zone 114: Reduction zone 115: Combustion Zone 116: Ash Grid Barrier 117: Ash Storage Tank 120: Built-in Combustion Pipe 121: Pore 122: Combustion Pipe 123: Exhaust Pipe 130: Gasification Air Pipe 140: High Pressure Air Blower 2: Biomass Carbonization Furnace 2 01 : Carbon material raw material 202 : Biomass energy carbon material 21 〇: carbonization furnace body 211 : carbonization zone 212 : drying zone 213 : cooling zone 220 : inlet port 230 : heat source input end 240 : heat source output end 250 : cooling end 260: discharge port 1321204 300: cooling unit 310: cooling fluid 400: automatic discharge unit 410: motor 420: conveyor belt
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