TW200916713A - Method and apparatus for drying pourable material - Google Patents
Method and apparatus for drying pourable material Download PDFInfo
- Publication number
- TW200916713A TW200916713A TW97136403A TW97136403A TW200916713A TW 200916713 A TW200916713 A TW 200916713A TW 97136403 A TW97136403 A TW 97136403A TW 97136403 A TW97136403 A TW 97136403A TW 200916713 A TW200916713 A TW 200916713A
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- Taiwan
- Prior art keywords
- drying
- dry
- silo
- adsorbent
- cargo
- Prior art date
Links
- 238000001035 drying Methods 0.000 title claims abstract description 49
- 238000000034 method Methods 0.000 title claims abstract description 32
- 239000000463 material Substances 0.000 title abstract description 5
- 239000003463 adsorbent Substances 0.000 claims abstract description 23
- 239000002274 desiccant Substances 0.000 claims abstract description 3
- 238000010276 construction Methods 0.000 claims description 7
- 238000001816 cooling Methods 0.000 claims description 6
- 238000010438 heat treatment Methods 0.000 claims description 4
- 230000001172 regenerating effect Effects 0.000 claims description 4
- 239000002594 sorbent Substances 0.000 claims description 3
- 238000007789 sealing Methods 0.000 claims description 2
- 238000000926 separation method Methods 0.000 claims 1
- 239000002893 slag Substances 0.000 claims 1
- 238000013022 venting Methods 0.000 claims 1
- 239000007789 gas Substances 0.000 description 16
- 230000008929 regeneration Effects 0.000 description 5
- 238000011069 regeneration method Methods 0.000 description 5
- 239000003795 chemical substances by application Substances 0.000 description 4
- 238000010586 diagram Methods 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 3
- 239000002808 molecular sieve Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 238000005192 partition Methods 0.000 description 2
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 241001465754 Metazoa Species 0.000 description 1
- 229920000426 Microplastic Polymers 0.000 description 1
- 241000282320 Panthera leo Species 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 239000005864 Sulphur Substances 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 238000005266 casting Methods 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 239000011888 foil Substances 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 238000004898 kneading Methods 0.000 description 1
- 230000007257 malfunction Effects 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 239000000344 soap Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- 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
- B01D53/26—Drying gases or vapours
- B01D53/261—Drying gases or vapours by adsorption
-
- 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
- B01D53/02—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 by adsorption, e.g. preparative gas chromatography
- B01D53/04—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 by adsorption, e.g. preparative gas chromatography with stationary adsorbents
- B01D53/0407—Constructional details of adsorbing systems
- B01D53/0431—Beds with radial gas flow
-
- 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
- B01D53/02—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 by adsorption, e.g. preparative gas chromatography
- B01D53/06—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 by adsorption, e.g. preparative gas chromatography with moving adsorbents, e.g. rotating beds
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B21/00—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
- F26B21/02—Circulating air or gases in closed cycles, e.g. wholly within the drying enclosure
- F26B21/04—Circulating air or gases in closed cycles, e.g. wholly within the drying enclosure partly outside the drying enclosure
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B21/00—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
- F26B21/06—Controlling, e.g. regulating, parameters of gas supply
- F26B21/08—Humidity
- F26B21/083—Humidity by using sorbent or hygroscopic materials, e.g. chemical substances, molecular sieves
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- General Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Analytical Chemistry (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Drying Of Solid Materials (AREA)
- Drying Of Gases (AREA)
Abstract
Description
200916713 六、發明說明: 【發明所屬之技術領域】 本發明係為在乾燥貯倉裡利用氣流使貨物乾燥(尤其是諸如 顆粒、粉末、晶粒、箔、碎片、塑料顆粒等固態物體)的方法及 構造;主要係顧自乾雜倉排出的廢流或喊在含有乾燥 劑/吸附劑的乾燥室裡弄乾,必要時使吸附劑再生,作為乾燥 流供貨物利用。 ’、’、 【先前技術】200916713 VI. Description of the Invention: [Technical Field of the Invention] The present invention is a method for drying goods (especially solid objects such as particles, powders, grains, foils, chips, plastic particles, etc.) by using a gas stream in a dry silo And the structure; mainly the waste stream discharged from the dry silo or shouting in a drying chamber containing a desiccant/adsorbent, and if necessary, regenerating the adsorbent as a dry stream supply. ',', [previous technology]
運用於使貨物乾燥的方法及構造創作有許多,如DE3625〇13 A1,揭路的疋利用乾燥空氣在乾燥漏斗弄乾塑料顆料的方法與器 ,。在4創作巾主要係為自乾㉟漏斗排出的廢氣在含有吸附劑的 乾燥機裡弄乾,再送回貨物作為乾燥空氣。 如DE197仍觀’揭露的是_弄乾貨物的空氣進行乾燥與 w…的方法與構造,其中該構造至少含有乾燥筒、下級空氣加熱 盗、下級乾燥貨物室及下級冷卻器材。 如刪118762Α卜揭露的是使含水氣的壓縮空氣再生的方 极=要係加熱大氣中的空氣,輸送至應再生的乾燥筒,利用乾 同θ再度冷卻,然在弄乾_空氣的触巾會有部分氣流漏出。 ^ EPG712656B1 ’揭露的是弄乾濕空氣的方法,及如Ερ7棚56 ,揭露的則是使含有濕氣的吸附劑再生的方法與構造。 、皮。如DE2025205A卜揭露的是在若干室裡選擇性吸附分子的構 駐f上述所有創作中所揭露的方法與構造皆具有下列共同缺 置—再生與錢時需耗費極多的能源,其構造的設備建 置而化費極高的金額。 造,Ϊϋ述缺失,本發日狀故研發出本案之方法及構 示了此即省能源外,還能有效降低成本花費。 【發明内容】 、 3 200916713 明係為在乾燥貯倉裡利用氣流使貨物乾燥的方法及構造 二2 f—乾燥室’該乾燥室的運作是以筒狀分為至少三個 '軸狀伸展的領域,其中吸附劑安排在___ =裡面__作為聽紐或絲㈣辭道;該管道 有吸附劑的領域相連,作為空氣通道。_上述設置轉流路 忐達成即使過程裡步驟不同但都只需用—個 $ 亦能降低投資總額與運作費用。 使用可命說來, 、 本發明還有另-_,就是運辦所需 不僅“有_硫的公能,雜有效降低費用成本。 _ t發明的設計亦朗不同產品及技術領域的需求而進行不同 材貝構件的置換’而能迎合不同產業的需求。 ° 較之=作=的乾燥室一軸端有底部,另-端有頂部, ί用⑽構,本創作的結構較簡單,價格亦較低廉。 個遠=明部上方設計有連結罩,在執行技術上亦只需要一 個連。罩’較之習用結構具有較佳的產業利用性。 (動,但連料狀科,縣軍與轉動 流路線技術’只需利用崎 是平結罩間’兩個相對的面至少有-面應 盤,彌補極二二要f可做為密封 中備===^伽歸峨,使用過程 3皁位,在使用過程中能獲得最佳控制。 4 200916713 再者,本發明不同部分間的分隔牆容易傾斜,若 计的噴射/>1力鑄造技術的優良措施,這項設計 氣= 線的擾亂滿流。 本發明依闕長至少設有三個(最好六個)區段 用過程不騎,顿朗單位使運作日__最佳総 = 筒的乾燥室不間斷地自行轉動,使過程裡不會發生故障。…、 *本發_®筒設計為至少—倾塊(最好五個)=亨 模組設計能以最簡單的方式使乾燥室能符合性能需求。 Μ 士發:中鄰近的區塊以頂部底部貯存至導槽彈簧的連接 樣簡易的技術設計確保個別要素間的穩定連接以及設#正 【實施方式】 其是士第一圖係為在乾燥貯倉1裡使貨物乾燥(尤 的流程圖、。主要係經由裝料2將貨物引進乾燥貯倉i ϋίΓΓ是用乾燥氣流3)使貨物乾燥(除去物料的水分)。自 乾無貝丁倉1經由吸料箱4使貨物乾燥,應驗鑄造機。 而自乾燥貯倉1排出的廢氣氣流5或回氣 =的乾燥室6裡弄乾,再作為乾燥氣流3運 將廢氣氣流經由過濾、器7與送風機8輸送至乾燥室 劑的輸送管’轉運至廢氣氣流5的乾燥室6,經過i附 :=;=,r乾燥貯倉1,其箭頭9== 、乾_氧如· 3 ‘入乾燥貯倉1前可以用加熱器10知、、田 :了再生吸_或分子細,雜騎线14 ^ 二 啟動過滤1112再啟動加鮮13。經過吸關或分子 200916713 行冷卻",以慮網再生或除11後,對吸附劑或分子遽網進 18漏出,作溫度,如此廢氣氣流5會有部分氣流 也會再二的吸附劑或分子濾網,這些部分氣流18 1丹?轉運(前碩19)到送風機8。 ,將廢Si?:乾三個範圍:第-個範圍係 子濾、網或吸附劑,第三個^^)^一個錢係為加熱或再生分 都能6依階段持續性轉動,所以每個領域裡 燥,=分子_或吸附劑的力二乾 成90。ί 點ίΓ : 一方面使氣流與輸送管裡的流動方向 ™第二次運送時藉由逆流減少能源消耗。 再生==,分)領域的氣流路線,可二網或 (再生細劑領域(含加熱與冷卻)的氣流路線。 第二圖係為本發明中乾燥室6的立體組人 .. 軸(圖中未顯示),該軸係設計在中 口〜圖,/、中有 設計是以筒狀分為至少:铜^處’ _燥室6的運作 子仙賴i则 卜轴狀伸展者,吸附劑或分 子濾網文排在中間的領域2〇,外面和裡 廢氣氣流5或乾燥氣流3的輸送管 員與21都作為 域20相連,作為空氣通道。;,有吸附劑的領 板和/或鑽孔板23產生連接,形成% 3、21 _由師 成軸狀排列,藉由跳板支樓成4通道’雜和/或鑽孔板 可稱=4=二了再以分隔牆— 了稱為至」)祕格樣式而言,依照周長至少設有三個區段(最 200916713 佳者為六個)。 作為圓筒的乾燥室設計至少有二個 結構第ί ==^部或_存至_^=處固邪。 弟一圖係為本發明整體設備的 牧处 定的連結㈣,如獅28上設有固 連結罩29與轉動圓筒「士、甘仁連結罩29固定不動, 29 有-個具彈性的平衡要素3G。 冑面應疋平的’至少 賴運糊輸送管的 明為排放管的領:流3的氣流再轉運到標 «21 > 輸达&>,IL動方向相反的方向排至該 嶋了細解圖 個範圍係將廢氣i j弄領域的範圍,第一 劑。刀子_或吸附劑’第三個範圍係為冷卻分子_或吸附 導弓提ill本方法及構造的特點是:依照逆流原理 守*?丨乾私至6的氣流路線,這麼一來轤叙 罩之間只有一個密封面。U來轉動圓商與固定不動的連接 【圖式簡單說明】 f圖.係為本發明之操作流程圖。 :係為本發明之乾燥㈣立方組合示意圖。 t圖.係為本發明之整體設備立體組合示音圖。 【主要元件符號說明】 " 乾燥貯倉1 裝料2 200916713 乾燥氣流3 廢氣氣流5 過濾器7、12 箭頭9 新鮮空氣14 廢氣15 吸料箱4 乾燥室6 送風機8 加熱器10、13 送風機11 換熱器16 箭頭17、19 氣流18 中間的領域(含有吸附劑的領域)20 裡面的領域(標明為排放管的領域)21 外面的領域(輸送管的領域)22 篩板或鑽孔板23 分隔牆24 區塊25 連接處26 底部27 頂部28 連結罩29 具彈性的平衡要素30There are many methods and constructions used to dry goods, such as DE 3625 〇 13 A1, a method and apparatus for drying plastic pellets in a drying funnel using dry air. In the 4 creation towel, the exhaust gas mainly discharged from the funnel 35 is dried in a dryer containing an adsorbent, and the goods are returned as dry air. As DE 197 still views, it is disclosed that the air of the cargo is dried and w... the structure contains at least a drying cylinder, a lower air heat thief, a lower dry cargo compartment and a lower cooling equipment. If the 118762 is deleted, the square pole that regenerates the compressed air of the water-containing gas is to be heated to the air in the atmosphere, sent to the drying cylinder to be regenerated, cooled again by the same θ, and then dried. Some airflow will leak out. ^ EPG712656B1 'Exposure is a method of drying wet air, and such as Ερ7 shed 56, revealing a method and construction for regenerating a moisture-containing adsorbent. ,skin. As disclosed in DE 2025 205 A, the structure and structure of the selectively adsorbed molecules in several chambers have the following common deficiencies in the above-mentioned various creations - regeneration and money require a lot of energy, and the constructed equipment A very high amount of money is spent on construction. The creation, the lack of description, the development of the case of this case and the construction of this case, which saves energy, can also effectively reduce costs. SUMMARY OF THE INVENTION, 3 200916713 The method is a method for drying goods by using airflow in a dry silo and a structure. The operation of the drying chamber is divided into at least three 'axial extensions in a cylindrical shape. The field in which the adsorbent is arranged in ___ = inside __ as a hearing button or wire (four) vocabulary; the pipe has a field of adsorbent connected as an air passage. _The above set of transfer routes 忐Achieve even if the steps in the process are different, but only use a $ can also reduce the total investment and operating costs. The use of life can be said, and the invention has another -_, that is, not only "has the sulphur's public energy, but also effectively reduces the cost. _ tInvented design also meets the needs of different products and technical fields. The replacement of different material shell members can meet the needs of different industries. ° Compared with the = dry = room, the bottom of the drying chamber has a bottom, the other end has a top, and the other uses a (10) structure. The structure of the creation is simple and the price is also It is cheaper. One far = the upper part of the upper part is designed with a joint cover, and only one connection is needed in the execution technology. The cover 'has better industrial utilization than the conventional structure. (moving, but the material section, the county army and Rotating flow route technology 'only need to use the Saki is a flat knot between the two opposite faces at least - face to disk, make up for the pole two to f can be used as a seal in the seal ===^ gamma, use process 3 The soap level can be optimally controlled during use. 4 200916713 Furthermore, the partition wall between different parts of the invention is easy to tilt, and if the injection/>1 force casting technique is excellent, the design gas = line The disturbance is full of flow. The invention has at least three It is best to have six sections. The process is not to ride. The unit is used to make the operation day __optimal 総 = the drying chamber of the cylinder rotates without interruption, so that no malfunction will occur in the process...., *本发__筒Designed to at least—dump block (preferably five)=Hang module design allows the drying chamber to meet performance requirements in the easiest way. Μ 士发: The middle adjacent block is stored at the top bottom to the guide spring connection Simple technical design to ensure stable connection between individual elements and set up [Implementation] The first figure is to dry the goods in the dry silo 1 (especially the flow chart, mainly through the charge 2 The goods are introduced into the dry silo i ϋ ΓΓ ΓΓ ΓΓ ΓΓ ΓΓ ΓΓ ΓΓ ΓΓ ΓΓ ΓΓ ΓΓ ΓΓ ΓΓ ΓΓ ΓΓ ΓΓ ΓΓ ΓΓ ΓΓ ΓΓ ΓΓ ΓΓ ΓΓ ΓΓ ΓΓ ΓΓ ΓΓ ΓΓ ΓΓ ΓΓ ΓΓ ΓΓ 货物 货物 货物 货物 货物 货物 货物 货物 货物 货物 货物 货物 货物 货物 货物 货物The exhaust gas stream 5 or the return air chamber 6 of the exhaust gas is dried, and then transported as a dry air stream 3 to transport the exhaust gas stream to the drying chamber of the drying chamber agent through the filter 7 and the blower 8 to the drying chamber of the exhaust gas stream 5 6, after i attached: =; =, r dry silo 1 , its arrow 9 ==, dry _ oxygen such as · 3 ' can be used to know the heater 10 before entering the dry silo 1 , Tian: regenerative suction _ or molecular fine, mixed riding line 14 ^ two start filter 1112 restart Fresh 13. After the suction or molecular 200916713 line cooling ", after the net regeneration or addition of 11, the adsorbent or molecular enthalpy into the 18 leakage, for the temperature, so the exhaust gas flow 5 will have some airflow will be two Adsorbent or molecular sieve, these partial gas streams 18 1 Dan? transport (pre-Shu 19) to the blower 8. Will waste Si?: dry three ranges: the first range is sub-filter, mesh or adsorbent, third ^^)^ A money for heating or regeneration can be 6 continuous rotation in stages, so dry in each field, = molecule _ or the force of the adsorbent is dried to 90.点 Point Γ : On the one hand, the flow direction in the air flow and the duct is reduced by the countercurrent to reduce energy consumption during the second transport. Regeneration ==, sub-) air flow route in the field, can be two mesh or (regeneration fine agent field (including heating and cooling) air flow route. The second figure is the three-dimensional group of drying chamber 6 in the present invention. Not shown in the middle), the shaft system is designed in the middle mouth ~ map, /, the design is divided into at least the tube: copper ^ ' _ dry room 6 operation son Xian Lai i then shaft-shaped stretcher, adsorption The agent or molecular sieve is arranged in the middle of the field 2, and the outside and inside of the exhaust gas stream 5 or the dry gas stream 3 are connected to the pipe 20 as the air passage. As the air passage, there is a sorbent collar and/or Or the drilled plate 23 is connected to form % 3, 21 _ arranged by the division in a shaft shape, and the four-channel 'hybrid and/or drilled plate can be said to be 4=two and then separated by the springboard. In terms of the secret style, there are at least three sections according to the circumference (the most is the best in 200916713). The drying chamber design as a cylinder has at least two structures: ί ==^ or _ stored at _^=. The picture of the younger brother is the link of the animal husbandry of the whole equipment of the invention (4). For example, the lion 28 is provided with a solid joint cover 29 and a rotating cylinder. The "shi, the genus connection cover 29 is fixed, and the 29 has a flexible balance. Element 3G. The surface of the kneading should be flattened at least as the leader of the delivery pipe: the flow of stream 3 is re-transferred to the standard «21 > Transmission &>, the direction of the IL is opposite So far, the range of the detailed solution is the range of the exhaust gas ij, the first agent. The third range of the knife _ or the adsorbent' is the cooling molecule _ or the adsorption guide ill. The method and structure are characterized. : According to the principle of counterflow, keep the airflow route to 6, so that there is only one sealing surface between the hoods. U to rotate the circular quotient and the fixed connection [simplified diagram] f diagram. The flow chart of the operation of the present invention is: a schematic diagram of the dry (four) cubic combination of the present invention. The figure is a three-dimensional combined sound diagram of the overall device of the present invention. [Main component symbol description] " Dry silo 1 Charge 2 200916713 Dry gas stream 3 Exhaust gas stream 5 Filter 7, 12 Arrow 9 Fresh Air 14 Exhaust gas 15 Suction box 4 Drying chamber 6 Blower 8 Heater 10, 13 Blower 11 Heat exchanger 16 Arrow 17, 19 Air flow 18 Intermediate area (area containing adsorbent) 20 Inside area (marked as discharge pipe Area) 21 Outside area (area of ducts) 22 Screen or drilled plate 23 Partition wall 24 Block 25 Connection 26 Bottom 27 Top 28 Connection cover 29 Elastic balance element 30
Claims (1)
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| AT15542007A AT505391B1 (en) | 2007-10-02 | 2007-10-02 | METHOD AND DEVICE FOR DRYING BULK GOODS |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| TW200916713A true TW200916713A (en) | 2009-04-16 |
Family
ID=40240444
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| TW97136403A TW200916713A (en) | 2007-10-02 | 2008-09-23 | Method and apparatus for drying pourable material |
Country Status (3)
| Country | Link |
|---|---|
| AT (1) | AT505391B1 (en) |
| TW (1) | TW200916713A (en) |
| WO (1) | WO2009043073A2 (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102893112A (en) * | 2010-03-03 | 2013-01-23 | 威特曼塑料仪器有限责任公司 | Devices for drying bulk materials |
| CN111482063A (en) * | 2020-04-22 | 2020-08-04 | 杭州腾睿源人防工程有限公司 | Filtering absorber |
Families Citing this family (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE102009049672A1 (en) | 2009-10-16 | 2011-04-28 | Fraunhofer-Gesellschaft zur Förderung der angewandten Forschung e.V. | Concept for generating experiences to update a reference database |
| AT509475B1 (en) * | 2010-03-03 | 2012-01-15 | Wittmann Kunststoffgeraete | METHOD FOR DRYING BULK GOODS |
| DE102010043087A1 (en) | 2010-10-28 | 2012-05-03 | Dürr Systems GmbH | Process chamber with device for injecting gaseous fluid |
| AT514153A1 (en) * | 2013-04-04 | 2014-10-15 | Wittmann Kunststoffgeräte Gmbh | Method for drying bulk material |
| WO2020247992A1 (en) | 2019-06-12 | 2020-12-17 | Wittmann Kunststoffgeräte Gmbh | Method for drying bulk materials, in particular solids, such as granulates, powders, grains, foils, shavings or the like, preferably plastic granulate |
| CN116853691B (en) * | 2023-06-09 | 2025-12-16 | 山东璟泰环保节能设备有限公司 | Dry denitration equipment feed bin assembly |
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|---|---|---|---|---|
| US2507607A (en) * | 1946-03-18 | 1950-05-16 | Ernest B Miller | Apparatus for conditioning air |
| US4176523A (en) * | 1978-02-17 | 1979-12-04 | The Garrett Corporation | Adsorption air conditioner |
| US4589892A (en) * | 1983-04-07 | 1986-05-20 | Bry-Air, Inc. | Sequenced modular bed carousel dehumidifier |
| JPS60178009A (en) * | 1984-02-25 | 1985-09-12 | Color Toronitsuku Kk | Method and apparatus for generation of high temperature dehumidified air for drying synthetic resin |
| DE3625013C2 (en) * | 1986-07-24 | 1995-05-24 | Somos Gmbh | Method and device for drying bulk goods, preferably made of plastic granules |
| US4805317A (en) * | 1987-11-13 | 1989-02-21 | Airflow Company | Microwave regeneration of adsorbent materials for reuse as drying agents |
| US5017202A (en) * | 1989-04-13 | 1991-05-21 | Taikisha Ltd. | Gas treating apparatus |
| US4974337A (en) * | 1989-10-30 | 1990-12-04 | The Conair Group, Inc. | Apparatus and method of drying and dehumidifying plastic |
| US5335426A (en) * | 1992-09-22 | 1994-08-09 | Foothills Medical Equipment, Inc. | Method and apparatus for thermal regeneration of molecular sieve material used in oxygen concentrators |
| DE4437494A1 (en) * | 1994-10-20 | 1996-04-25 | Graeff Roderich Wilhelm | Method and device for drying moist gas |
| DE19757537A1 (en) * | 1997-12-23 | 1999-07-08 | Wittmann Kunststoffgeraete Gmb | Method and device for drying and heating air for drying solids |
| ITVR20030053A1 (en) * | 2003-05-05 | 2004-11-06 | Moretto Plastics Automation S R L | MOLECULAR SIEVES EQUIPMENT AND DEHUMIDIFICATION SYSTEM |
| ITVR20060030A1 (en) * | 2006-02-10 | 2007-08-11 | Moretto Spa | SYSTEM AND DEHUMIDIFICATION PROCEDURE WITH FLEXIBLE OPERATION PARTICULARLY FOR GRANULAR MATERIALS. |
-
2007
- 2007-10-02 AT AT15542007A patent/AT505391B1/en not_active IP Right Cessation
-
2008
- 2008-09-23 TW TW97136403A patent/TW200916713A/en unknown
- 2008-10-02 WO PCT/AT2008/000354 patent/WO2009043073A2/en not_active Ceased
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102893112A (en) * | 2010-03-03 | 2013-01-23 | 威特曼塑料仪器有限责任公司 | Devices for drying bulk materials |
| CN102893112B (en) * | 2010-03-03 | 2015-04-01 | 威特曼塑料仪器有限责任公司 | Apparatus for drying bulk materials and method of use thereof |
| CN111482063A (en) * | 2020-04-22 | 2020-08-04 | 杭州腾睿源人防工程有限公司 | Filtering absorber |
| CN111482063B (en) * | 2020-04-22 | 2022-03-08 | 杭州腾睿源人防工程有限公司 | Filtering absorber |
Also Published As
| Publication number | Publication date |
|---|---|
| WO2009043073A2 (en) | 2009-04-09 |
| AT505391B1 (en) | 2009-01-15 |
| AT505391A4 (en) | 2009-01-15 |
| WO2009043073A3 (en) | 2009-08-13 |
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