M361381 五、新型說明： 【新型所屬之技術領域】 本創作係有關一種輸送吸附材之調整式吹送器，尤指 一種藉由調整内部間隙而控制吸附材之供給量，俾以調整 出最佳化之吸附材輸送流量，進而產生最佳吸附能力之設 計者。 【先前技術】 按，如第一圖所示，流體化床（F1 uidi zed bed)吸附濃 縮系統，搭配管殼式冷凝單元之廢氣淨化處理流程，係為 VOCs(Volatile Organic Compounds)廢氣經由製程風車（鼓 風機，11)抽送進入吸附塔（Adsorber，10)底下之分散部 (Distributor，12)，期使氣流在吸附塔内均勻地流動 (Uniform flow);而吸附塔（10)内部以多孔平板（Tray，13) 分隔成數層（一般四至六層），並讓直徑約0.7mm之真球狀 活性碳成為吸附材（30)，而由吸附塔（10)頂端落下，活性 碳吸附材（30)則因氣流之作用而在多孔平板（13)上方形成 2〜3公分之流體化浮動層，並沿著多孔平板（13) —層一層 地逐一落下，形成流體化床活性碳之均勻浮動之吸附程 序；當活性碳吸附材（30)與含有VOCs廢氣接觸時，數以千 萬計之活性碳吸附材（30)可將VOCs有效吸附，氣體淨化後 由塔頂排放。 接著，當吸附飽和之活性碳吸附材（30)落至吸附塔（10) 底部貯槽（14)後，則可藉輸送裝置（20)之輸送氣源（21)， 以所送出之空氣或氮氣形成推送力，經連接第一吹送器（22) M361381 與第一分離器（23)之管路送至脫附塔（40)頂端，並進入脫 附塔（40)内進行無氧環境再生程序，再生後之活性碳吸附 材（30)則以連接第二吹送器（24)與第二分離器（25)之管路 送回吸附塔（10)的頂端；而脫附出來的高濃度廢氣（一般濃 縮倍率為1000〜10000倍左右），則以氮氣氣流經管路送至 冷凝塔（Condenser，50)，進行降溫冷凝成液體回收或直接 送入燃燒機氧化分解，如此形成一連續操作之VOCs去除程 序。另外，一般應用於氣體乾燥除濕之流體化床乾燥系統， 工作流程與前述VOCs去除程序相同。 次按，欲藉由流體化床淨化之廢氣及一般欲乾燥處理 氣體之溫度、溼度、吸附材物理特性、氣體組成特性、濃 度及吸附塔（10)内部多孔平板（13)之隔層數…等特性，均 會影響吸附材（30)之吸脫附能力及吸脫附速度，故吸附材 (30)之輸送流量必須配合前述之各種特性予以調整；而習 知調整吸附材（30)輸送流量之方式，係以控制該輸送裝置 (20)之輸送氣源（21)之供氣量予以調整，但因輸送氣源（21) 供氣量之控制難以微調，致使吸附材（30)輸送流量之調整 精準度較差。 【新型内容】 本創作之主要目的，係欲提供一種輸送吸附材之調整 式吹送器，而具有提升吸附材輸送流量調整精準度之功效。 為達上述功效，本創作之結構特徵，係包括有： 一導氣座，内部形成有出氣口朝上之氣流通道，且於 該出氣口周緣形成承接吸附材之承接面，而該氣流通道之 進氣口與外部輸送氣源連接； M361381 一斜三通管，將其直管底端接合於該導氣座頂端，而 其斜官用以供吸附材落至該直管；以及 — 插e藉由升降機構組裝於該直管頂端之密封環 “讓插s底端對準该氣流通道之出氣口，且與該承接面 保持有供吸附材通過之間隙，致使落至該直管與插管兩管 j間之吸附材’由該承接面承接且陸續因重力與氣流流速 生低壓吸引力作用被導引至該出氣口，並被自該出氣口 導出之氣流，從該插管管内向上吹送者。 此外，該升降機構為螺栓搭配一對固定螺帽與一對調 整螺帽，而由該對固定螺帽將螺栓組裝於該密封環蓋，且 令該插皆形成有穿設於螺栓之凸緣，並藉樓托於該 調f螺帽，調整該插管之升降狀態。X，該直管底端與導 =座頂端相對形成有接合凸緣，並纽—密封墊片而予以 论封接σ另’該承接面為外高内低之斜面型態。再 =環蓋尚包括有抽承或密封材與軸承定位環，而該密 、”、、石墨、四氟乙烯盤根纖維、鐵氟龍、橡膠、矽膠或 其他潤滑性密封材料。 / 【實施方式】 首先，請參閱第二圖所示，本創作係包括有： 導氣座（6G)’内部形成有出氣口（6⑴朝上之氣流通 道（61)，錄該出氣口（6⑴周緣形成承接吸附材⑽之承 接面（62) ’並令該承接面⑽為外高内低之斜面型離，俾 將吸附材⑽向該出氣口（6⑴導引，而該氣流通道⑽之 進氣口（612)與外部輪送氣源（圖未示）連接； M361381 一斜三通管（70)，將其直管（71)底端接合於該導氣座 (60)頂端，而其斜管（72)用以供吸附材（30)落至該直管 (71);其中，該直管（71)底端與導氣座（60)頂端相對形成 有接合凸緣（73、63)，並夾設一密封墊片（64)而予以密封 接合；以及 一插管（80)，藉由升降機構（81)組裝於該直管（71)頂 端之密封環蓋（74)，讓插管（80)底端對準該氣流通道（61) 之出氣口（611) ’且與該承接面（62)保持有供吸附材（3〇)通 過之間隙（d)，致使落至該直管（71)與插管（80)兩管壁間之 吸附材（30) ’由該承接面（62)承接且陸續因重力作用被導 引至該出氣口（611)，並被自該出氣口（611)導出之氣流， 從該插管（80)管内向上吹送者。 此外，該升降機構（81)為螺栓（811)搭配一對固定螺帽 (812)與一對調整螺帽（813) ’而由該對固定螺帽（812)將螺 栓（811)組裝於該密封環蓋（74)，且令該插管（8〇)形成有穿 設於嫘栓（811)之凸緣（82)，並藉撐托於該凸緣（82)之調整 螺帽（813) ’調整ό亥插官.（80)之升降狀態；又，該密封環蓋 (74)尚包括有軸承或密封材（741)與定位環（742)，讓該插 管（80)之升降更具順暢性；而該密封材（741)為石墨、四敦 6烯盤根纖維、鐵氟龍、橡膠、矽膠或其他潤滑性密封材 料。 基於如是之構成’本創作係將用以輸送吸附材之吹送 器，讓其吸附材供給量由原本之固定式改進為調整式；而 本創作之調整方式，乃藉由該升降機構（81)調整該插管（8〇) 之升降狀態，亦即調整該插管（80)底端與該承接面（62)之 M361381 間隙（d)，進而控制吸附材之供給量；是以，本創作調整吸 附材供給量之設計方式，可因應流體化床吸附濃縮系統所 欲處理之VOCs廢氣，其溫度、溼度、組成特性、濃度及吸 附塔結構…等特性，調整出最佳化之吸附材輸送流量（氣固 比），而產生最佳之吸附能力，乃具有提升吸附材輸送流量 調整精準度之功效。 綜上所述，本創作所揭示之構造，為昔所無，且確能達 到功效之增進，並具可供產業利用性，完全符合新型專利要 件，祈請貴審查委員核賜專利，以勵創新，無任德感。 惟，上述所揭露之圖式、說明，僅為本創作之較佳實施 例，大凡熟悉此項技藝人士，依本案精神範疇所作之修飾或 等效變化，仍應包括在本案申請專利範圍内。 M361381 【圖式簡單說明】 第一圖係流體化床吸附濃縮系統之結構說明圖。 第二圖係本創作之結構剖示圖。 【主要元件符號說明】M361381 V. New description: [New technical field] This is a type of adjustable blower for transporting adsorbent materials, especially one that controls the supply of adsorbent material by adjusting the internal clearance. The adsorbent material transports the flow rate, which in turn produces the designer of the best adsorption capacity. [Prior Art] According to the first figure, the fluidized bed (F1 uidi zed bed) adsorption concentration system, combined with the exhaust gas purification process of the shell-and-tube condensing unit, is VOCs (Volatile Organic Compounds) exhaust gas through the process windmill (Blower, 11) is pumped into the dispersion (Distributor, 12) under the adsorption tower (Adsorber, 10), so that the gas flow is uniformly flowed in the adsorption tower (Uniform flow); and the inside of the adsorption tower (10) is a porous plate ( Tray, 13) is divided into several layers (generally four to six layers), and the true spherical activated carbon having a diameter of about 0.7 mm is made into the adsorbent material (30), and is dropped from the top end of the adsorption tower (10), and the activated carbon adsorbing material (30) Then, a fluidized floating layer of 2 to 3 cm is formed on the porous plate (13) by the action of the gas flow, and falls down one by one along the porous plate (13) to form a uniform floating adsorption of the fluidized bed activated carbon. Procedure; when the activated carbon adsorbing material (30) is in contact with the VOCs-containing exhaust gas, tens of millions of activated carbon adsorbing materials (30) can effectively adsorb the VOCs, and the gas is purified and discharged from the top of the tower. Then, when the adsorbed saturated activated carbon adsorbing material (30) falls to the bottom storage tank (14) of the adsorption tower (10), the gas source (21) can be transported by the conveying device (20) to deliver the air or nitrogen. Forming a pushing force, which is sent to the top of the desorption column (40) through a pipeline connecting the first blower (22) M361381 and the first separator (23), and enters the desorption tower (40) for an oxygen-free environment regeneration process. The regenerated activated carbon adsorbing material (30) is sent back to the top end of the adsorption tower (10) by a line connecting the second blower (24) and the second separator (25); and the desorbed high-concentration exhaust gas (General concentration ratio is about 1000~10000 times), it is sent to the condensation tower (Condenser, 50) through the pipeline by nitrogen gas flow, and is cooled and condensed into liquid recovery or directly sent to the combustion machine for oxidative decomposition, thus forming a continuously operated VOCs. Remove the program. In addition, it is generally applied to a fluidized bed drying system for gas drying and dehumidification, and the workflow is the same as the aforementioned VOCs removal procedure. Sub-press, the temperature and humidity of the exhaust gas to be purified by the fluidized bed and the general processing gas to be dried, the physical properties of the adsorbent, the gas composition characteristics, the concentration, and the number of layers of the porous plate (13) inside the adsorption tower (10)... The characteristics of the adsorption material (30) will affect the adsorption and desorption capacity and the adsorption and desorption rate. Therefore, the delivery flow rate of the adsorption material (30) must be adjusted in accordance with the above various characteristics; and the conventional adsorption material (30) is adjusted. The flow rate is adjusted by controlling the gas supply amount of the conveying gas source (21) of the conveying device (20), but it is difficult to finely adjust the gas supply amount of the conveying gas source (21), so that the adsorbing material (30) delivers the flow rate. The adjustment accuracy is poor. [New content] The main purpose of this creation is to provide an adjustable blower for conveying the adsorbent material, and to improve the accuracy of the transport flow adjustment of the adsorbent material. In order to achieve the above effects, the structural features of the present invention include: a gas guiding seat, an air flow passage having an air outlet upward is formed therein, and a receiving surface for receiving the adsorbing material is formed at a periphery of the air outlet, and the air flow passage is The air inlet is connected to the external conveying air source; M361381 an oblique tee pipe, the bottom end of the straight pipe is joined to the top end of the air guiding seat, and the oblique officer is used for the adsorption material to fall to the straight pipe; and - inserting e The sealing ring assembled at the top end of the straight pipe by the lifting mechanism "aligns the bottom end of the inserting s with the air outlet of the air flow passage, and maintains a gap with the receiving surface for the adsorbing material to pass through, so as to fall into the straight pipe and insert The adsorbing material between the two tubes j is supported by the receiving surface and is guided to the air outlet by gravity and air flow velocity, and is extracted from the air outlet from the air inlet. In addition, the lifting mechanism is a bolt with a pair of fixing nuts and a pair of adjusting nuts, and the pair of fixing nuts assemble the bolts to the sealing ring cover, and the plugs are formed to be threaded on the bolts Flange and borrow The adjusting nut is adjusted to adjust the lifting state of the cannula. X, the bottom end of the straight pipe is formed with a joint flange opposite to the top end of the guide seat, and the sealing ring is sealed and the other is the sealing surface. It is a low-profile bevel type. The ring cover also includes a suction or sealing material and a bearing positioning ring, and the dense, ",, graphite, tetrafluoroethylene packing fiber, Teflon, rubber, silicone rubber Or other lubricious sealing materials. / [Embodiment] First, please refer to the second figure. This creation includes: The air guide seat (6G) has an air outlet (6 (1) upward airflow passage (61), and the air outlet (6 (1)) The peripheral edge is formed to receive the receiving surface (62) of the adsorbing material (10) and the supporting surface (10) is an outer high and a low inclined surface type, and the adsorbing material (10) is guided to the air outlet (6 (1), and the air flow passage (10) is advanced. The air port (612) is connected with an external circulating air source (not shown); the M361381 is an oblique tee tube (70), and the bottom end of the straight tube (71) is joined to the top end of the air guiding seat (60), and the inclined portion thereof The tube (72) is configured to drop the adsorbing material (30) to the straight tube (71); wherein the bottom end of the straight tube (71) is formed with an engaging flange (73, 63) opposite to the top end of the air guiding seat (60). And sealingly engaging a sealing gasket (64); and a cannula (80), a sealing ring cover (74) assembled on the top end of the straight pipe (71) by a lifting mechanism (81), allowing insertion The bottom end of the tube (80) is aligned with the air outlet (611)' of the air flow passage (61) and the gap (d) for the passage of the adsorbing material (3〇) is maintained with the receiving surface (62), causing the falling to The adsorbing material (30) between the straight pipe (71) and the cannula (80) is received by the receiving surface (62) and is guided to the air outlet (611) by gravity, and is The air outlet derived from the air outlet (611) is blown upward from the inside of the cannula (80). Further, the lifting mechanism (81) is a bolt (811) with a pair of fixing nuts (812) and a pair of adjusting nuts ( 813) 'The bolt (811) is assembled to the seal ring cover (74) by the pair of fixed nuts (812), and the cannula (8〇) is formed with a flange that is threaded on the peg (811) (82), and by adjusting the adjusting nut (813) of the flange (82) to adjust the lifting state of the cymbal (80); further, the sealing ring cover (74) further includes a bearing or The sealing material (741) and the positioning ring (742) make the lifting and lowering of the cannula (80) more smooth; and the sealing material (741) is graphite, Si Dun 6-ene packing fiber, Teflon, rubber, Silicone or other lubricious sealing material. Based on the composition of the present invention, the blowing device for conveying the adsorbent material will be improved from the original fixed type to the adjusted type; The adjustment method of the creation is to adjust the lifting state of the cannula (8〇) by the lifting mechanism (81), that is, to adjust the gap between the bottom end of the cannula (80) and the M361381 of the receiving surface (62) (d) And further controlling the supply amount of the adsorbent material; therefore, the design method of adjusting the supply amount of the adsorbent material according to the present invention can respond to the VOCs exhaust gas to be treated by the fluidized bed adsorption and concentration system, and its temperature, humidity, composition characteristics, concentration and adsorption tower The characteristics of the structure, etc., adjust the optimized adsorption material transport flow rate (gas-solid ratio), and produce the best adsorption capacity, which has the effect of improving the accuracy of the adsorption flow adjustment of the adsorbent material. In summary, the structure revealed by this creation is unprecedented, and it can achieve the improvement of efficacy, and it can be used for industrial utilization. It fully complies with the new patent requirements, and invites your review committee to grant patents. Innovation, no sense of morality. However, the above-mentioned drawings and descriptions are only preferred embodiments of the present invention. Modifications or equivalent changes made by those skilled in the art in accordance with the spirit of the case should still be included in the scope of the patent application. M361381 [Simple description of the diagram] The first diagram is a structural diagram of the fluidized bed adsorption concentration system. The second figure is a structural cross-sectional view of the present creation. [Main component symbol description]
(10)吸附塔 (62)承接面 (11)製程風車 (63)接合凸緣 (12)分散部 (64)密封墊片 (13)多孔平板 (70)斜三通管 (14)貯槽 (71)直管 (20)輸送裝置 (72)斜管 (21)輸送氣源 (73)接合凸緣 (22)第一吹送器 (74)密封環蓋 (23)第一分離器 (741)密封材 (24)第二吹送器 (742)定位環 (25)第二分離器 (80)插管 (30)吸附材 (81)升降機構 (40)脫附塔 (811)螺栓 (50)冷凝塔 (812)固定螺帽 (60)導氣座 (813)調整螺帽 (61)氣流通道 (82)凸緣 (611)出氣口 (d)間隙 (612)進氣口(10) adsorption tower (62) bearing surface (11) process windmill (63) joint flange (12) dispersion part (64) gasket (13) porous plate (70) oblique tee (14) storage tank (71 Straight pipe (20) conveying device (72) inclined pipe (21) conveying gas source (73) engaging flange (22) first blowing device (74) sealing ring cover (23) first separator (741) sealing material (24) second blower (742) positioning ring (25) second separator (80) cannula (30) adsorbent material (81) lifting mechanism (40) desorption tower (811) bolt (50) condensation tower ( 812) fixed nut (60) air bearing seat (813) adjusting nut (61) air flow channel (82) flange (611) air outlet (d) gap (612) air inlet