TW200404603A - Material fine-graining device and method for using the device - Google Patents

Material fine-graining device and method for using the device Download PDF

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Publication number
TW200404603A
TW200404603A TW092123776A TW92123776A TW200404603A TW 200404603 A TW200404603 A TW 200404603A TW 092123776 A TW092123776 A TW 092123776A TW 92123776 A TW92123776 A TW 92123776A TW 200404603 A TW200404603 A TW 200404603A
Authority
TW
Taiwan
Prior art keywords
cylinder
sleeve
circular plate
opened
raw material
Prior art date
Application number
TW092123776A
Other languages
Chinese (zh)
Other versions
TWI289471B (en
Inventor
Tomihisa Naito
Original Assignee
Naito Syouko
Tomihisa Naito
Tokai Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Naito Syouko, Tomihisa Naito, Tokai Corp filed Critical Naito Syouko
Publication of TW200404603A publication Critical patent/TW200404603A/en
Application granted granted Critical
Publication of TWI289471B publication Critical patent/TWI289471B/en

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Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/40—Static mixers
    • B01F25/42—Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions
    • B01F25/421—Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions by moving the components in a convoluted or labyrinthine path
    • B01F25/422—Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions by moving the components in a convoluted or labyrinthine path between stacked plates, e.g. grooved or perforated plates
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/40—Static mixers
    • B01F25/44—Mixers in which the components are pressed through slits
    • B01F25/441—Mixers in which the components are pressed through slits characterised by the configuration of the surfaces forming the slits
    • B01F25/4412—Mixers in which the components are pressed through slits characterised by the configuration of the surfaces forming the slits the slits being formed between opposed planar surfaces, e.g. pushed again each other by springs
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/40—Static mixers
    • B01F25/44—Mixers in which the components are pressed through slits
    • B01F25/441—Mixers in which the components are pressed through slits characterised by the configuration of the surfaces forming the slits
    • B01F25/4416—Mixers in which the components are pressed through slits characterised by the configuration of the surfaces forming the slits the opposed surfaces being provided with grooves
    • B01F25/44165—Radial grooves formed on opposed surfaces, e.g. on planar surfaces
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/40—Static mixers
    • B01F25/45—Mixers in which the materials to be mixed are pressed together through orifices or interstitial spaces, e.g. between beads
    • B01F25/452—Mixers in which the materials to be mixed are pressed together through orifices or interstitial spaces, e.g. between beads characterised by elements provided with orifices or interstitial spaces
    • B01F25/4521—Mixers in which the materials to be mixed are pressed together through orifices or interstitial spaces, e.g. between beads characterised by elements provided with orifices or interstitial spaces the components being pressed through orifices in elements, e.g. flat plates or cylinders, which obstruct the whole diameter of the tube
    • B01F25/45211—Mixers in which the materials to be mixed are pressed together through orifices or interstitial spaces, e.g. between beads characterised by elements provided with orifices or interstitial spaces the components being pressed through orifices in elements, e.g. flat plates or cylinders, which obstruct the whole diameter of the tube the elements being cylinders or cones which obstruct the whole diameter of the tube, the flow changing from axial in radial and again in axial

Landscapes

  • Chemical & Material Sciences (AREA)
  • Dispersion Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Disintegrating Or Milling (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)

Abstract

In a material atomizing device (12) for graining a pressurized raw material, a main casing (17) and extension casings (18a, 18b, 18c) are arranged in sequence in line within a tube body (16). Each of the casings (17, 18a, 18b, 18c) has an axial passage (22) connected to a hollow chamber (20) through hole portions (21). One end of the axial passage (22) is closed, and the other end is connected to an exit portion. In the main casing (17), an inlet portion (14) of the tube body (16) is connected to the hollow chamber (20). In the extension casings (18a, 18b, 18c), each hollow chamber (20) is connected an exit portion (23) of the preceding casing through a communication passage (24). In the casing (18c) at the end, the exit portion (23) is connected to an outlet (15) of a cover portion (30).

Description

200404603 ⑴ _ 玖、發明說明 【發明所屬之技術領域】 本發明，是關於一種將食品、化學、醫藥等的各業界 使用的物質微粒化的裝置，特別是關於能夠得到乳化、分 散、攪拌或打碎物質後微粒化成微米單位或以下之均勻（ 或均質）的粒子直徑後，安定的粒度分怖的裝置。同時， 本發明係關於使用微粒化裝置來處理引擎機油等的廢油後 做成燃料的方法。 % 【先前技術】 如大家習知，一般使用 APV式考琳均化器（Courlene homogenizer)當做傳統的物質之微粒化裝置。此一裝置， 係做成在於閥座的一端的開口處，將閥面對閥座的構成來 形成擁有極小的間隙。這種構成的目的，係從閥座的另一 端的開口利用高壓傳送過來的原料經過前述間隙噴出到閥 的半徑方向外側後，藉由衝擊到衝擊環的內側壁來微粒化 φ 且均質化原料中的物質。在這種裝置中，利用調節前述間 隙後將原料的處理壓力設定在數1 07Pa後能夠得到所期望 的處理量 （l〇t/h)。 同時，其他傳統的物質之微粒化裝置而言，有大家習 知的利用擁有孔徑的細管、或擁有多數個節流孔（小孔）的 發生器（裝置本體）之微粒化加壓原料的裝置（請參閱日本 特許第3 00243 2號）。 進一步’爲了改善上述兩個傳統的裝置，有日本特願 288 (2) (2)200404603 2000-181600號所提示的物質之微粒化裝置。 此一裝置，係由筒體與在筒體的內面上能夠滑動的內 筒構成。筒體，係分別在於一端側的側面具備供應原料到 內筒的入口部，在另一端具備排出被微粒化的原料到裝置 外部的出口部。內筒，係被配置成沿著筒體的軸方向。在 於內筒的側壁，形成貫通到內筒的中空部之由多數個群集 所形成的多數孔。在此，相同群集擁有相同的孔徑。 在於微粒化處理的情形下，利用設置在內筒的一端的 操作元件來移動內筒後，使用適合原料中的物質之粒度大 小的孔徑的群集來對向入口部。接著，利用高壓供應原料 到入口部後，介隔著屬於對向著入口部之群集的多數孔， 引導原料到內筒的中空部。 經過此一處理的過程，原料中的物質在各孔的內部， 利用被加高壓的原料液體受到剝離的現象所產生的真空泡 沫分裂時發生的衝擊波來微粒化後，從出口部排出到裝置 外部。因此，將上述的微粒處理移動在筒內後邊依序改變 孔徑的大小並且多數次反覆處理後，能夠得到所希望的處 理量及粒度分佈。 上述的裝置，係針對改善兩個傳統的裝置，做成對應 原料中的物質之粒度大小而不需更換發生器之具備多數發 生器的功能。但是，在於上述裝置，由於每經過一次微粒 化處理，只要擁有特定的孔徑的一個群集來微粒化的緣故 ，必須依次改變孔徑的大小多數次地反覆微粒化處理才能 夠達到所預期的處理量及粒度分怖。隨之，由於再度將各 * - 6 - (3) (3)200404603 次微粒化處理後排出的原料供應到入口部的原因，必需要 有連結出口部與入口部的附屬裝置。因此，在於多樣化、 泛用性、簡單化、及製造·性的觀點上被認爲必需進一步地 改善裝置。 本發明，係有鑑於上述的實情所提出，目的是提供一 種利用一次的微粒化處理能夠達成所預期的處理量及粒度 分佈’將原料微粒化、均質化，並且採取簡單的構成的物 質之微粒化裝置。進一步，本發明的另一個目的，係提供 一種使用本發明的物質之微粒化裝置來處理引擎機油等的 廢油當做燃料的方法。 【發明內容】 爲了達成上述目的，本發明，係在於微粒化被加壓後 送來的原料的物質之微粒化裝置，具備：封閉一端而將另 一端開口的筒體；及爲了封閉前述筒體的另一端而被鎖入 到前述另一端的蓋部；及爲了引導前述原料到裝置內部而 設置在前述筒體的吸入口部·，及在於前述筒體的內部，被 連接到前述吸入口部後，因應被設置在內部的孔徑之噴嘴 特性來微粒化前述原料的主套筒·，及在於前述筒體內部， 將被依序並列設置，且因應設置在內部的孔徑之噴嘴特性 ’進一步地微粒化主套筒內被微粒化的原料之多數個接續 用套筒；及爲了排出前述多數個接續用套筒微粒化的原料 到裝置外部而設置在前述蓋部的中央部之吐出口部。 根據本發明’使用主套筒與多數個接續用套筒，能夠 (4) (4)200404603 經過多次地將原料微粒化的緣故，能力利用一次微粒化處 理獲得所希望的處理量及粒度分佈。 本發明的最佳實施方式，係前述主套筒具備：外筒； 及封閉擁有沿著軸方向形成後將兩端開口的出口部之前述 外筒的一端的第1圓板；及封閉前述外筒的另一端用的第 2圓板；及夾在封閉一端後在前述出口部的一端打開另一 端之前述第1圓板與第2圓板之間且被固定在前述外筒的 內部之內筒，在於前述內筒與前述外筒之間形成中空室後 ，前述吸入口部的端部在前述中空部開口後，在於前述內 筒的側面，於前述中空室將一端開口，並且沿著前述內筒 的直徑方向形成在前述內筒的中空部將另一端開口之多數 個前述孔。 依據這種方式，在於設置在內筒的壁側的多數個孔， 藉由送入被加壓的原料，能夠根據各個孔的噴嘴特性將原 料微粒化的緣故，因此藉由簡單的構成能夠實現原料的微 粒化。 本發明的最佳實施方式，係前述接續用套筒具體：外 筒；及封閉擁有沿著軸方向形成後將兩端開口的出□部之 前述外筒的一端的第1圓板；及封閉擁有沿著軸方向形成 後將兩端開口的連通路之前述外筒的另一端的第3圓板； 及夾在封閉一端後在前述出口部的一端打開另一端之前述 第1圓板與第3圓板之間且被固定在前述外筒的內部之內 筒，在於前述內筒與前述外筒之間形成中空室後，前^胃 通路的一端在前述中空部開口後，在於前述內筒的側面， -8- 291 (5) (5)200404603 於前述中空室將一端開口，並且沿著前述內筒的直徑方向 形成在前述內筒的中空部將另一端開口之多數個前述孔。 依據這種方式，·在於設置在內筒的壁側的多數個孔， 藉由送入被加壓的原料’能夠根據各個孔的噴嘴特性將原 料微粒化的緣故，因此藉由簡單的構成能夠實現原料的微 粒化。同時，利用逐次減小各接續用套筒的孔徑，形成能 夠發生適合原料中的物質之粒度大小的衝擊波的緣故，能 夠有效率地實現原料的微粒化。 本發明的最佳實施方式，係爲了在於對向前述第2圓 板的前述第1圓板的一端端面，收容前述內筒的一端，形 成凹陷與前述內筒相同直徑之規定深度的第1凹部，且爲 了在於對向前述第1圓板的前述第2圓板的一端端面，收 容前述內筒的另一端，形成凹陷與前述內筒相同直徑之規 定深度的第2凹部。 依據這種方式，利用分別卡合內筒的兩端部到第1圓 板及第2圓板，形成內筒被固定在外筒的緣故，能夠簡單 地製作主套筒。 本發明的最佳實施方式，係爲了在於對向前述第3圓 板的前述第1圓板的一端端面，收容前述內筒的一端，形 成凹陷與前述內筒相同直徑之規定深度的第1凹部，爲了 在於對向前述第1圓板的前述第3圓板的一端端面，收容 前述內筒的另一端的緣故，形成凹陷與前述內筒相同直徑 之規定深度的第3凹部。 依據這種方式，利用分別卡合內筒的兩端部到桌1圓 -9- 292 (6) (6)200404603 板及第3圓板，形成內筒被固定在外筒的緣故，能夠簡單 地製作接續用套筒。 本發明的最佳實施方式，係前述連通路由：設置在前 述第3凹部的底面之溝槽部；及在於相鄰接的套筒之前述 第1圓板的出口部之另一端將一端開口，且在於前述溝槽 部將另一端開口的供應部；及在於前述溝槽部將一端開口 ，且在於前述中空室將另一端開口之貫通孔所形成。 依據這種方式，利用簡易的構成，形成能夠確實地從 相鄰接的套筒輸送原料到接續用套筒。 本發明的最佳實施方式，係前述溝槽部，係以前述的 供給部之開口部爲中心，將前述第3凹部的底面設置成放 射狀。 依據這種方式，由於多數條溝槽被形成在第3凹部的 底面的緣故，能夠有效率地從相鄰接的套筒傳送原料到接 續用套筒。 本發明的最佳實施方式，係前述連通路由：對向著丰目 鄰接的套筒之前述第1圓板的出口部之另一端，且設置# 前述第3圓板的另一端端面之溝槽部；及在於前述溝槽部 將一端開口，且在於前述中空室將另一端開口之貫通孔所 形成。 依據這種方式，由於從相鄰接的套筒輸送出來的原_ 不會直接地打到內筒的緣故，能夠更安定地固定外筒！^ @ 筒。 本發明的最佳實施方式，係介隔著由設置在前述第 -10- (7) (7)200404603 圓板的一端端面之溝槽部；及在前述溝槽部將一端開口且 在於前述中空室將另一端開口之貫通孔所形成的連通孔， 形成前述吸入口的端部在前述中空室開口。 ， 依據這種方式，由於主套筒與接續用套筒的構成相同 的緣故，形成能夠簡單地製作套筒。 爲了達到上述目的，本發明，係在於微粒化被加壓後 輸送過來的原料之物質之微粒化裝置，具備：封閉一端而 打開另一端的筒體；及爲了封閉前述的筒體的另一端而設 置在前述筒體的另一端的蓋部；及爲了導入前述原料到裝 置內部而設置在前述筒體的吸入口部；及在於前述筒體的 內部，被連接到前述吸入口部後，因應被設置在內部的孔 徑之噴嘴特性來將前述原料微粒化的主套筒；及在前述筒 體的內部，將被依序並排設置，且因應設置在內部的孔徑 之噴嘴特性，進一步地微粒化前述主套筒微粒化的原料之 多數個接續用套筒；及排出前述多數個接續用套筒微粒化 的原料之排出套筒；及爲了將前述排出套筒所排出的原料 排出到裝置外部而設置在前述蓋部的中央部之吐出口部。 依據本發明，能夠因應所期望的處理量以及粒度的分 怖來改變接續用套筒的數量的緣故，本發明的微粒化裝置 更具備有效的對應性。 爲了達成上述的目的，本發明，係使用將擁有由入口 部、孔部、及出口部所形成的流體通路之套筒多數並排設 置在擁有吸入口部及吐出口部的筒體的內部後，連接最先 的套筒的入口部到前述吸入口部，並且依序地連接前述最 -11 - (8) (8)200404603 先的套筒之出口部到下一個套筒的入口部，並連接最後一 個套筒的出口部到前述吐出口部的微粒化裝置後，做成處 理廢油來當做燃料的處理方法，其特徵爲：對廢油加上i 〇 至50%重量的水來做成原料後，利用高壓泵浦將前述原料 加壓後，輸送前述被加壓的原料到前述吸入口後，依序將 原料微粒化成對應設置在各套筒的內部之前述孔部的噴嘴 特性的粒度，並且從前述吐出口將被微粒化成適當的粒度 之前述原料取出來當做乳化燃料。 依據本發明，因應各套筒的孔的噴嘴特性，將原料微 粒化的緣故，在於廢油與水屬於分子的狀態下能夠獲得混 合且充分的乳液化，進而能夠得到所期望的燃料。 【實施方式】 如第1圖所示，供給到原料供給口 1 0的原料會經由 高壓幫浦（壓力1 0 6至1 0 7 P a的柱塞型）1 1加壓後，送到微 粒化裝置（發生器）1 2。接著，原料在微粒化裝置1 2被 微粒化後經過通路L，當做微粒製品被取出到承接器1 3。 依照這種流程，能夠加工原料成微粒化製品。 佐以第2圖至第1 8圖說明和本發明相關的物質之微 粒化裝置的第1至第4竇施方式。進一步地，佐以第1 9 圖至第21圖說明第1實施方式所示的物質之微粒化裝置 的使用例。在於本實施方式中，分別朝微粒化裝置1 2的 長方形方向、上下方向、以及寬度方向當做X軸、Y軸、 Z軸。此外，X軸、Y軸、Z軸的相互間形成正交。200404603 ⑴ _ 玖, description of the invention [Technical field to which the invention belongs] The present invention relates to a device for atomizing substances used in various industries such as food, chemistry, medicine, etc., and in particular, it can be emulsified, dispersed, stirred or beaten. After crushing the material, it is micronized into uniform (or homogeneous) particle diameters in micron units or less, and a stable particle size distribution device. Meanwhile, the present invention relates to a method of using a micronization device to treat waste oil such as engine oil, and to prepare a fuel. % [Prior art] As everyone knows, APV type Courlene homogenizer is generally used as the traditional material micronization device. This device is formed by the valve seat facing the valve seat at the opening at one end of the valve seat to form a small gap. The purpose of this structure is to pulverize φ and homogenize the material by impacting the raw material transferred from the opening at the other end of the valve seat by high pressure through the gap to the outside of the valve in the radial direction, and impacting the inner side wall of the impact ring Substance. In such a device, a desired processing amount (10 t / h) can be obtained by setting the processing pressure of the raw material after the gap is adjusted to 107 Pa. At the same time, as for other conventional micronization devices for materials, there are conventional devices that use micronized tubes with pores or generators (device bodies) with a large number of orifices (small holes) to pressurize raw materials. (See Japanese Patent No. 3 00243 2). Further, in order to improve the above two conventional devices, there is a device for atomizing a substance as suggested in Japanese Patent Application No. 288 (2) (2) 200404603 2000-181600. This device is composed of a cylinder and an inner cylinder which can slide on the inner surface of the cylinder. The cylinders each have an inlet portion for supplying raw materials to the inner cylinder on the side surface on one end side, and an outlet portion for discharging the particulate material to the outside of the device at the other end. The inner cylinder is arranged along the axial direction of the cylinder. In the side wall of the inner tube, a plurality of holes formed by a plurality of clusters are formed so as to penetrate through the hollow portion of the inner tube. Here, the same clusters have the same aperture. In the case of micronization, after the inner cylinder is moved by using an operation element provided at one end of the inner cylinder, a cluster of pore sizes suitable for the particle size of the substance in the raw material is used to face the inlet. Next, after the raw material is supplied to the inlet by high pressure, the raw material is guided to the hollow portion of the inner cylinder through a plurality of holes belonging to the cluster facing the inlet. After this process, the material in the raw material is micronized in the interior of each hole by using the shock wave generated when the vacuum foam is split due to the phenomenon that the high-pressured raw material liquid is stripped, and then discharged from the outlet to the outside of the device. . Therefore, by moving the above-mentioned fine particle treatment inside the cylinder and sequentially changing the size of the pore size and repeating the treatment many times, the desired amount of treatment and particle size distribution can be obtained. The above-mentioned device is aimed at improving two conventional devices, and is made to correspond to the particle size of the material in the raw material without having to replace the generator. It has the function of most generators. However, in the above-mentioned device, since each time the micronization process is performed, as long as a cluster having a specific pore size is used for micronization, the size of the pore size must be changed in order to repeat the micronization process many times to achieve the expected processing capacity and Granularity distribution. Accordingly, since the raw materials discharged after each *-6-(3) (3) 200404603 micronization treatment were supplied to the inlet portion again, it was necessary to have an accessory device connecting the outlet portion and the inlet portion. Therefore, it is considered necessary to further improve the device from the viewpoints of diversification, versatility, simplification, and manufacturability. The present invention has been made in view of the above-mentioned facts, and an object thereof is to provide fine particles of a substance capable of achieving a desired processing amount and particle size distribution by using one-time micronization treatment to 'pulverize and homogenize raw materials and adopt a simple structure化 装置。 The device. Furthermore, another object of the present invention is to provide a method for treating waste oil such as engine oil as a fuel using a micronization device of the substance of the present invention. [Summary of the Invention] In order to achieve the above object, the present invention is a micronization device for micronizing a material that is sent after being pressurized, and includes a cylinder closed at one end and opened at the other end; The other end is locked to the cover portion of the other end; and the suction port portion provided in the cylinder to guide the raw material to the inside of the device is connected to the suction port portion inside the cylinder. Then, the main sleeve of the raw material is micronized according to the nozzle characteristics of the aperture provided inside, and the inside of the cylinder body will be sequentially arranged side by side, and the nozzle characteristics of the aperture provided inside will be further A plurality of splicing sleeves of the micronized raw material in the micronized main sleeve; and a discharge port provided at a central portion of the cover portion in order to discharge the plurality of micronized materials of the splice sleeve to the outside of the apparatus. According to the present invention, 'the main sleeve and the plurality of splicing sleeves can be used to (4) (4) 200404603 because the raw material can be atomized several times, and the ability to obtain a desired treatment amount and particle size distribution can be achieved by using a single particle treatment . According to a preferred embodiment of the present invention, the main sleeve includes: an outer cylinder; and a first circular plate that closes one end of the outer cylinder having an exit portion that is opened at both ends after being formed along the axial direction; and the outer casing is closed. A second circular plate for the other end of the tube; and between the first circular plate and the second circular plate which are opened at one end of the outlet portion after being closed at one end and fixed inside the outer tube After the hollow chamber is formed between the inner cylinder and the outer cylinder, the end of the suction port portion is opened in the hollow portion, and a side of the inner cylinder is opened at one end of the hollow chamber, and the The diameter direction of the inner cylinder is formed in the plurality of holes in the hollow portion of the inner cylinder to open the other end. According to this method, since a large number of holes provided on the wall side of the inner cylinder are fed with a pressurized raw material, the raw material can be atomized according to the nozzle characteristics of each hole. Therefore, it can be realized with a simple structure. Micronization of raw materials. The best embodiment of the present invention is the above-mentioned splicing sleeve specifically: an outer cylinder; and a first circular plate that closes one end of the outer cylinder having an outlet portion that is opened at both ends after being formed along the axial direction; and a closure A third circular plate having the other end of the outer cylinder having a communication path opened at both ends after being formed along the axial direction; and the first circular plate and the first circular plate opened at the other end at one end of the exit portion after being closed at one end 3 The inner tube between the circular plates and fixed inside the outer tube is that after a hollow chamber is formed between the inner tube and the outer tube, one end of the front stomach passage is opened in the hollow portion, and then the inner tube is in the inner tube. On the side, -8-291 (5) (5) 200404603 opens one end in the hollow chamber, and forms a plurality of the aforementioned holes in the hollow portion of the inner cylinder along the diameter direction of the inner cylinder to open the other end. According to this method, since a large number of holes provided on the wall side of the inner cylinder are fed with the pressurized raw material, the raw material can be atomized according to the nozzle characteristics of each hole. Therefore, a simple structure can be used. Achieving atomization of raw materials. At the same time, the pore diameter of each of the splicing sleeves is successively reduced to form a shock wave capable of generating a particle size suitable for the substance in the raw material, and the raw material can be efficiently atomized. A preferred embodiment of the present invention is to face the one end surface of the first disc facing the second disc to receive one end of the inner cylinder to form a first recess having a predetermined depth of the same diameter as the inner cylinder. In order to face the one end surface of the second disc facing the first disc, the other end of the inner cylinder is accommodated, and a second recessed portion having a predetermined depth and the same diameter as the inner cylinder is formed. According to this method, the main sleeve can be easily manufactured by engaging the both ends of the inner tube to the first disc and the second disc to form the inner tube to be fixed to the outer tube. The preferred embodiment of the present invention is to face the one end face of the first disc of the third disc to receive one end of the inner cylinder to form a first recessed portion having a predetermined depth of the same diameter as the inner cylinder. In order to receive the other end of the inner cylinder so as to face the one end surface of the third disc facing the first disc, a third recess having a predetermined depth having the same diameter as the inner cylinder is formed. According to this method, the ends of the inner tube are respectively engaged to the table 1 circle -9- 292 (6) (6) 200404603 plate and the third circular plate, so that the inner tube is fixed to the outer tube, so it can be simply Make a splicing sleeve. The best embodiment of the present invention is the aforementioned communication route: a groove portion provided on the bottom surface of the third recessed portion; and the other end of the exit portion of the first circular plate of the adjacent sleeve is opened at one end, It is formed by a through hole in which the other end of the groove portion is opened; and a through hole in which the one end of the groove portion is opened and the other end is opened in the hollow chamber. In this way, with a simple structure, it is possible to form a material capable of reliably conveying the raw material from the adjacent sleeve to the splicing sleeve. A preferred embodiment of the present invention is the aforementioned groove portion, and the bottom surface of the third recessed portion is provided in a radial shape with the opening portion of the aforementioned supply portion as the center. According to this method, since a plurality of grooves are formed on the bottom surface of the third recessed portion, it is possible to efficiently transfer the raw material from the adjacent sleeve to the connection sleeve. The best embodiment of the present invention is the aforementioned communication route: the other end of the exit portion of the first circular plate facing the sleeve adjacent to Fengme is provided, and a groove portion of the end surface of the other end of the third circular plate is provided And a through hole formed by opening one end of the groove portion and opening the other end by the hollow chamber. According to this method, since the original conveyed from the adjacent sleeves will not directly hit the inner cylinder, the outer cylinder can be more stably fixed! ^ @Tube. The preferred embodiment of the present invention is provided through a groove portion provided on one end surface of the aforementioned -10- (7) (7) 200404603 circular plate; and one end is opened in the groove portion and lies in the hollow. A communication hole formed by a through hole opened at the other end of the chamber to form the end of the suction port opens in the hollow chamber. According to this method, since the configuration of the main sleeve and the connection sleeve is the same, the sleeve can be easily manufactured. In order to achieve the above-mentioned object, the present invention is a micronization device for micronizing a raw material that is conveyed after being pressurized, and includes a cylinder closed at one end and opened at the other end; A cover portion provided at the other end of the cylinder body; and a suction port portion provided in the cylinder body to introduce the raw material into the device; and the inside of the cylinder body connected to the suction mouth portion in response to being The main sleeve of the inside diameter of the nozzle set to atomize the raw material; and the inside of the cylinder will be arranged side by side in order, and the nozzle will be further micronized according to the nozzle characteristics of the inside diameter of the inside. A plurality of splicing sleeves for the raw material of which the main sleeve is atomized; and a discharge sleeve for discharging the plurality of sparged materials for the use of the preceding sleeve; and provided to discharge the raw material discharged from the discharge sleeve to the outside of the device A spout at a central portion of the cover portion. According to the present invention, the number of splicing sleeves can be changed in accordance with the desired processing amount and particle size distribution, and the micronization device of the present invention has more effective correspondence. In order to achieve the above-mentioned object, the present invention uses a sleeve having a fluid passage formed by an inlet portion, a hole portion, and an outlet portion to be installed side by side in a cylinder having a suction port portion and a discharge port portion. Connect the inlet of the first sleeve to the suction port, and sequentially connect the outlet of the previous -11-(8) (8) 200404603 to the inlet of the next sleeve and connect After the outlet part of the last sleeve reaches the above-mentioned micronization device of the discharge outlet part, it is made into a method for treating waste oil as fuel, which is characterized by adding i 0 to 50% by weight of water to the waste oil. After the raw materials, the high-pressure pump is used to pressurize the raw materials, and then the pressurized raw materials are conveyed to the suction port, and then the raw materials are sequentially atomized into particle sizes corresponding to the nozzle characteristics of the hole portions provided inside the respective sleeves. In addition, the raw material which is micronized into an appropriate particle size from the aforementioned outlet is taken out as an emulsified fuel. According to the present invention, in accordance with the characteristics of the nozzles of the holes of each sleeve, the raw materials are micronized, so that a mixed and sufficient emulsion can be obtained in a state where the waste oil and water are molecules, and a desired fuel can be obtained. [Embodiment] As shown in FIG. 1, the raw material supplied to the raw material supply port 10 is sent to the microparticles after being pressurized through a high-pressure pump (a plunger type having a pressure of 106 to 107 Pa).化 装置 (Generator) 1 2. Next, the raw material is micronized in the micronization device 12 and passes through the passage L, and is taken out as a micronized product to the receiver 13. According to this process, raw materials can be processed into micronized products. Figs. 2 to 18 are used to describe the first to fourth sinus administration methods of the microgranulation device of the substance related to the present invention. Further, an example of using the device for atomizing a substance shown in the first embodiment will be described with reference to FIGS. 19 to 21. In this embodiment, the X-axis, Y-axis, and Z-axis are taken as the rectangular direction, the up-down direction, and the width direction of the micronization device 12, respectively. The X-axis, Y-axis, and Z-axis are orthogonal to each other.

29S -12- (9) (9)200404603 (第1實施方式） 微粒化裝置12，係如第2圖所示，具備：吸入口 1 4、 吐出口 1 5 _"、筒體1 6、主套筒！ 7、第1接續用套筒.| 1 8 a、 第2接續用套筒18b、第3接續用套筒18c、及蓋子30。 筒體16，係屬於硬質不銹鋼製，被做成圓筒形狀。 筒體16的一端（-X)被封閉，另一端（ + X)呈開口。吸入口 14，係如第3圖所不’被設置在筒體1 6的一端側的側面 來供給原料到微粒化裝置1 2的內部。吐出口 1 5，係如第 4圖所示，被設置在螺合在筒體16的另一端的蓋子30的 中央來排出被微粒化的原料到微粒化裝置1 2的外部。 在於筒體16的內部，從筒體16的一端朝+χ方向依 主套筒17、第1接續用套筒18a、第2接續用套筒18b、 第3接續用套筒1 8c的順序排列。主套筒1 7，係被配置 在吸入口部1 4的下部，接續用套筒1 8c則連接到蓋子3 0 〇 主套筒17，係具備：入口部19、中空室20、多數個孔 部21、軸方向通路22、出口部23、外筒25、以及內筒 26。外筒25’係屬於硬質不銹鋼製，在內部擁有陶瓷製 的內筒26，且形成主套筒1 7的外觀。入口部1 9，係形成 吸入口 1 4以及外筒2 5，用來供給原料到中空室2 0。 中 空室20，係被形成在外筒25 ;及封閉與外筒25同心的一 端（-X側）之內筒26之間。多數個孔部21，爲了做成沿著 內筒2 6的軸方向（X軸），做成並設在內筒2 6的側面後， 分別沿著內筒2 6的直徑方向延伸。孔部2 1的一端對向著 -13- (10) (10)200404603 中空室20開口，另一端對向著軸方向通路22開口。軸方 向通路22，係屬於內筒26的中空部，軸方向通路22的 一端（-X側）被封閉，另一端（+ X側）則對向著出口部23開 □。 第1接續用套筒18a、第2接續用套筒18b、第3接 續用套筒1 8 c，係分別具備：中空室2 0、多數個孔部2 1、 軸方向通路22、出口部23、連通路24、外筒25及內筒 2 6。外筒2 5，係屬於硬質不銹鋼製，在內部擁有陶瓷製 的內筒26，且形成第1接續用套筒18a、第2接續用套筒 18b、及第3接續用套筒18c的外觀。中空室20，係被形 成在使用圓板元件來封閉兩端的外筒2 5，及封閉與外筒 2 5同心的一端（-X側）之內筒2 6之間。多數個孔部2 1，爲 了做成沿著內筒2 6的軸方向（X軸），做成並設在內筒2 6 的側面後，分別沿著內筒2 6的直徑方向延伸。孔部2 1的 一端，係對向著中空室20開口，另一端則對向著軸方向 通路22開口。軸方向通路22，係屬於內筒26的中空部 ，軸方向通路22的一端（-X側）被封閉，另一端（+ X側）則 對向著出口部23的一端（-X側）開口。連通路24，的一端 (-X側），係對向著從-X側相鄰接的套筒延伸設置的出口 部23(供給部）的另一端開口，另一端（+ X側）則對向著中 空室20開口。此外，第3接續用套筒18c的出口部23的 另一端（+ X側），係對向著蓋子30的吐出口 15的另一端（-X側）開口。 佐以第5圖及第9圖說明關於主套筒1 7的外筒25與29S -12- (9) (9) 200404603 (First embodiment) The micronization device 12 is provided with a suction port 1 4, a discharge port 1 5 _ ", a cylinder 16, and a main body, as shown in FIG. 2. Sleeve! 7. The first splicing sleeve. | 1 8 a, the second splicing sleeve 18b, the third splicing sleeve 18c, and the cover 30. The cylinder 16 is made of hard stainless steel and has a cylindrical shape. One end (-X) of the cylinder 16 is closed, and the other end (+ X) is open. The suction port 14 is provided on the side surface on the one end side of the cylinder 16 as shown in Fig. 3 to supply raw materials into the inside of the micronization device 12. As shown in Fig. 4, the discharge port 15 is provided at the center of the lid 30 screwed to the other end of the cylinder 16 to discharge the micronized material to the outside of the micronization device 12. It is located inside the cylinder 16 and is arranged in the order of the main sleeve 17, the first connection sleeve 18a, the second connection sleeve 18b, and the third connection sleeve 18c from the one end of the tube 16 in the + χ direction. . The main sleeve 17 is disposed below the suction port portion 14 and the connection sleeve 18c is connected to the cover 300. The main sleeve 17 is provided with an inlet portion 19, a hollow chamber 20, and a plurality of holes. The part 21, the axial direction passage 22, the exit part 23, the outer cylinder 25, and the inner cylinder 26. The outer cylinder 25 'is made of hard stainless steel, has an inner cylinder 26 made of ceramic, and forms the appearance of the main sleeve 17. The inlet portion 19 forms a suction port 14 and an outer cylinder 25, which are used to supply raw materials to the hollow chamber 20. The hollow chamber 20 is formed between the outer tube 25 and the inner tube 26 which closes one end (-X side) concentric with the outer tube 25. The plurality of hole portions 21 are formed along the axial direction (X axis) of the inner tube 26 to form side surfaces of the inner tube 26, and then extend in the diameter direction of the inner tube 26, respectively. One end of the hole portion 21 opens toward the -13- (10) (10) 200404603 hollow chamber 20, and the other end opens toward the axial direction passage 22. The axial direction passage 22 belongs to the hollow portion of the inner cylinder 26. One end (-X side) of the axial direction passage 22 is closed, and the other end (+ X side) is opened toward the outlet portion □. The first splicing sleeve 18a, the second splicing sleeve 18b, and the third splicing sleeve 1 8c are respectively provided with a hollow chamber 20, a plurality of hole portions 21, an axial direction passage 22, and an exit portion 23. , Communication path 24, outer tube 25 and inner tube 26. The outer cylinder 25 is made of hard stainless steel and has an inner cylinder 26 made of ceramic. The outer cylinder 25 has the appearance of a first connection sleeve 18a, a second connection sleeve 18b, and a third connection sleeve 18c. The hollow chamber 20 is formed between an outer cylinder 25 which is closed at both ends by a circular plate element, and an inner cylinder 26 which is closed at one end (-X side) concentric with the outer cylinder 25. The plurality of hole portions 21 are formed along the axial direction (X axis) of the inner tube 26, and are formed and provided on the side surfaces of the inner tube 26, respectively, and extend along the diameter direction of the inner tube 26. One end of the hole portion 21 is opened toward the hollow chamber 20 and the other end is opened toward the axial passage 22. The axial direction passage 22 belongs to the hollow portion of the inner tube 26. One end (-X side) of the axial direction passage 22 is closed, and the other end (+ X side) is opened toward the end (-X side) facing the outlet portion 23. One end (-X side) of the communication path 24 is opened toward the other end of the outlet portion 23 (supply portion) extending from the sleeve adjacent to the -X side, and the other end (+ X side) is opposite The hollow chamber 20 is opened. In addition, the other end (+ X side) of the outlet portion 23 of the third connection sleeve 18c is open to the other end (-X side) of the outlet 15 facing the cover 30. The outer tube 25 and the outer sleeve 25 of the main sleeve 17 are described with reference to FIGS. 5 and 9.

-14 - (11) 200404603 內筒26的連接肩造。 如第5圖所示，在於主套筒1 7，爲了封閉外筒2 5的 兩端在於該兩端鎖入第1圓板3 1及第2圓板3 2。更詳 細地說，利用分別鎖入設置在第1圓板31及第2圓板3 2 的螺絲孔，封閉外筒2 5的兩端。此外，兩塊圓板中，也 可以做成一塊圓板被直接地焊接在外筒2 5的端部的內面 ，另一塊圓板被直接地螺合在外筒2 5的端部的內面。-14-(11) 200404603 The connecting shoulder of the inner cylinder 26. As shown in Fig. 5, the two ends of the main sleeve 17 are used to close the outer cylinder 25, and the first disc 31 and the second disc 32 are locked at the two ends. More specifically, both ends of the outer tube 25 are closed by screw holes provided in the first circular plate 31 and the second circular plate 32, respectively. In addition, of the two circular plates, one circular plate may be directly welded to the inner surface of the end of the outer cylinder 25, and the other circular plate may be directly screwed to the inner surface of the end of the outer cylinder 25.

在於主套筒1 7的第1圓板3 1的一端端面（-X側），係 如第9圖所示，爲了收容主套筒17的內筒26的另一端 (+ X側），形成凹陷與內筒26相同直徑之規定深度的凹部 3 7。同時，在於第1圓板3 1的中央部，沿著X軸設置出 口部23。在於主套筒17的第2圓板32的另一端端面（+ X 側），爲了收容主套筒17的內筒26的一端（-X側），形成 凹焰與內筒26相同直徑之規定深度的凹部3 9。The one end surface (-X side) of the first circular plate 31 of the main sleeve 17 is formed as shown in FIG. 9 to accommodate the other end (+ X side) of the inner tube 26 of the main sleeve 17 The recess 37 having a predetermined depth having the same diameter as the inner tube 26 is recessed. At the same time, an outlet portion 23 is provided along the X axis in the center portion of the first circular plate 31. On the other end face (+ X side) of the second circular plate 32 of the main sleeve 17, in order to accommodate one end (-X side) of the inner tube 26 of the main sleeve 17, a concave flame is formed with the same diameter as the inner tube 26 Depth of recess 3 9.

在於主套筒1 7的內筒2 6的另一端（+ X側），設置密 封墊27，且內筒26，係被插入在第1圓板31的凹部37 與第2圓板3 2的凹部3 9之間後，一體式地被固定在外筒 25的內部。利用這種構造，內筒26，不僅不會受到筒體 1 6作用到外筒2 5之鎖付外壓的影響，又形成不洩漏原料 的處理液之密閉的中空室20。中空室20，係介隔著多數 個孔部2 1被連接到軸方向通路22。此外，由於在軸方向 通路22與出口部23的連接處（座面2 8)的附近設置密封墊 27的緣故，原料處理液不會洩漏。 佐以第5圖、第9圖以及第10圖說明在於第1接續 -15- (12) (12)200404603 用套筒18a的外筒25與內筒26。 在於第1接續用套筒1 8 a，爲了能夠封閉外筒2 5的 兩端，在其兩端處鎖入第1圓板3 1及第3圓板3 3。詳述 之，藉由分別螺合設置在第1圓板3 1及第2圓板3 2的側 面的螺絲部；與設置在外筒25的兩端部之內面的螺絲孔 來封閉外筒2 5的兩端。兩塊圓板中，也可以做成一塊圓 板被直接地焊接在外筒25的端部的內面，另一塊圓板被 直接地螺合在外筒25的端部的內面。 在於第1接續用套筒1 8a的第1圓板3 1的一端端面 ，會與主套筒1 7的第1圓板3 1相同形成凹部3 7。同時 ，在於第1圓板3 1，沿著X軸設置出口部2 3。在於第1 接續用套筒18a的第3圓板33的另〜端端面（+ X側），如 第10圖所示，爲了收容第1接續用套筒18a的內筒26的 一端（-X側），形成凹陷與內筒26相同直徑之規定深度的 凹部以。 第3圓板3 3的中央部，係沿著X軸，擁有從主套筒 1 7延伸設置的出口部23 (供給部）。此外，此一部份稱之 爲供給部。在於第3圓板3 3的凹部3 8的座面29，形成 沿著Y軸延伸的溝槽部3 4。從主套筒1 7延伸設置的出口 部2 3的另一端（+ X側），係對向著溝槽部3 4開口。同時 ，在於溝槽部3 4的上下端部，連通沿著X軸所形成的貫 通孔3 5到溝槽部3 4。利用溝槽部3 4與貫通孔3 5構成連 通路24。 在於第1接續用套筒1 8 a的內筒2 6的另一端（+ X側） -16- 299 (13) (13)200404603 ，設置密封墊27，且內筒26，係被插入在第1圓板31的 凹部3 7與第3圓板3 3的凹部3 8之間後，一體式地被固 定在外筒25的內部。利用這種構造，內筒26，不僅不會 受到筒體1 6作用到外筒2 5的鎖付外壓的影響，又形成不 洩漏原料的處理液之密閉的中空室2 0。此外，由於在軸 方向通路22與出口部23的連接處的周圍設置密封墊27 的緣故，原料處理液不會洩漏。 如上述所構成的主套筒1 7及第1接續用套筒1 8 a， 係藉由將主套筒17的第1圓板31對向著第1接續用套筒 1 8 a的第3圓板3 3形成相互連結在一起。此外，爲了能 夠在正確的位置上連接主套筒17與第1接續用套筒18a ，分別在第1圓板3 1與第3圓板3 3設置收容突起部的收 容溝槽40 (請參閱第8圖）。藉由這種構造，能夠簡單地連 結主套筒1 7與第1接續用套筒1 8 a。 在於第2接續用套筒18b及第3接續用套筒18c，外 筒25與內筒26，係如第6圖及第7圖所不’利用與第1 接續用套筒1 8 a相同的構造來連結在一起。 同時，第1接續用套筒18a及第2接續用套筒18b， 係藉由將第1接續用套筒1 8a的第1圓板3 1對向著第2 接續用套筒18b的第3圓板33，形成相互連結在一起。 此外，爲了能夠在正確的位置上連接第1接續用套筒1 8 a 與第2接續用套筒1 8b，分別在第1圓板與第3圓板設置 收容突起部的收容溝槽40 (請參閱第8圖）°藉由這種構造 ，能夠簡單地連結第1接繪用套細1 8 a與桌2接續用套筒 •17- (14) (14)200404603 1 8b 〇 相同地，第2接續用套筒18b及第3接續用套筒18.c ，係藉由將第1接續用套筒1 8b的第1圓板3 1對向著第 3接續用套筒18c的第3圓板33，形成相互連結在一起。 此外，爲了能夠在正確的位置上連接第2接續用套筒18b 與第3接續用套筒1 8 c，分別在第1圓板與第3圓板設置 收容突起部的收容溝槽40 (請參閱第8圖）。藉由這種構造 ，能夠簡單地連結第2接續用套筒1 8b與第3接續用套筒 1 8c 〇 進一步，藉由連結主套筒1 7到吸入口 1 4，形成連結 主套筒1 7到筒體1 6。藉由連結第3接續用套筒1 8 c到吐 出口 15，形成連結第3接續用套筒18c到蓋子30。 在於各套筒的多數個孔部2 1的孔徑，係被設定成朝 + X方向隨著增加套筒的數量而減小。這是因爲在於孔部 2 1的內部產生符合原料中的物質的粒度之衝擊波。同時 ，也可以因應需求，做成在於各套筒的多數個孔部2 1的 所有孔徑也都可以相同。進一步，在於一個套筒中，也可 以任意地改變多數個孔部2 1的孔徑。藉此，能夠得到擁 有多數個山峰的粒度分佈。 在於第1實施方式中，雖然將接續用套筒的數量做成 3個，但是能夠因應所期望的處理數量及粒度分佈來改變 其數量。例如，如第11圖所示，在於將接續用套筒的數 量做成2個的情形下，從筒體1 6取下蓋子3 0後，只要將 第V接續用套筒18c取代在中央部僅具備的出口部46之 •18- 301 (15) (15)200404603 接續用套筒4 7即可。當增加接續用套筒的數量時，只要 插入所.期望的數量之新設的接續.用套筒到筒體1.6與蓋子 3 〇之間即可。 ·- 第1實施方式，係如第1 0圖所示，在於第3圓板3 3 的凹部3 8的座面2 9，沿著Y軸形成一個溝槽部3 4。但 是’溝槽部3 4的設置並不限定如此，也可以如第1 2圖所 示’以出口部23的開口面爲中心延伸成放射狀來形成多 數條溝槽部3 4。這種情形下，在於溝槽部3 4的兩端部， 連通沿著X軸所形成的貫通孔3 5到各溝槽部3 4。藉此， 能夠有效率地送出原料到相鄰接的套筒。 在於第1實施方式，如第1 〇圖所示，貫通孔3 5係隔 著凹部3 8所形成。但是，貫通孔3 5的設置並不在此限， 如第1 3圖所示，也可以去掉凹部3 8的側面的一部份來形 成貫通孔3 5。 在於第1實施方式，係如第5圖至第7圖所示，在於 主套筒17，鎖入第1圓板3 1及第2圓板3 2到外筒2 5的 兩端後，在於第1接續用套筒18a、第2接續用套筒18b 、及第3接續用套筒1 8 c，鎖入第1圓板31及第3圓板 3 3到外筒2 5的兩端。但是，封閉各套筒的外筒的兩端的 方法並不被限定如此，也可以形成如第1 4圖所示的方法 。換句話說，去掉外筒2 5的兩端部的外面後，在於凹陷 的外面設置螺絲部的同時，將第1圓板121、第2圓板 122、及第3圓板123形成袋子狀’且在於對向著外筒25 的螺絲部的內面設置螺絲孔。接著，藉由螺合外筒2 5的 -19- (16) (16)200404603 螺絲部與各圓板,的螺絲孔來封閉外筒2 5的兩端。耢此’‘ 能夠確實地密封外筒2 5的兩端的同時’能夠輕易地從外 筒2 5鬆脫裝著各圓板。 (第2實施方式） 第2實施方式的微粒化裝置7 〇，係如第1 5圖所示’ 形成溝槽部的部份與第1實施方式的微粒化裝置12不同 。其他的微粒化裝置7 0的構成，係與第1實施方式的微 Φ 粒化裝置12的構成相同。此外，選用與第1實施方式相 同的構成之元件則給予相同的符號。 在於第1實施方式中，溝槽部3 4 ’係被形成在設置 在第3圓板33的另一端端面（+ X側）的凹部38的座面29 。在於第2實施方式中，溝槽部52，係被形成在設置在 第3圓板3 3的一端端面（-X側）。在於溝槽部52的兩端， 連通沿著X軸所形成的貫通孔54。藉由溝槽部52與貫通 孔54構成連通路50。 修 在於第3圓板33，在於未收容內筒26側（-X側）的端 面，藉由形成溝槽部5 2，形成從出口部2 3送出的原料不 會直接地打到內筒26的緣故，外筒25與內筒26的固定 變得非常安定。 同時，如第16圖所示，若設置吸入口 60在筒體16 的一端的話，能夠將所有的構成做成一樣。因此，能夠更 容易地製作微粒裝置。 除了上述的變形例以外，也能夠將第1實施方式中說 -20- 383 (17) (17)200404603 明過的變形例適用在第2實施方式的微粒化裝置7 〇上。 (第3實施方式） 第3實施方式的微粒化裝置9 0，係如第1 7圖所示， 形成溝槽部的部份與第1實施方式的微粒化裝置1 2不同 。其他的微粒化裝置的構成，係與第1實施方式的微粒化 裝置1 2的構成相同。此外，選用與第1實施方式相同的 構成之元件則給予相同的符號。 在於第1實施方式中’溝槽部3 4，係被形成在設置 在第3圓板33的另一端端面（+ Χ側）的凹部38的座面29 。在於第3實施方式中，溝槽部8 2 ’係被形成在-X側所 鄰接的套筒的第1圓板3 1的另一端端面（+ Χ側）。在於溝 槽部8 2的兩端部，連通形成在+Χ側所鄰接的接續用套筒 的第3圓板的貫通孔84。藉由溝槽部82與貫通孔84構 成連通路80。 藉由在於-X側所鄰接的套同之弟1圓板3 1形成溝槽 部8 2，形成從出口部2 3送出的原料不會直接地打到內筒 26的緣故，外筒25與內筒26的固定變得非常安定。 此外，能夠將第1實施方式中說明過的變形例適用在 第3實施方式的微粒化裝置90上。 (第4實施方式） 第4實施方式的微粒化裝置1 1 〇，係如第1 8圖所示 ，各接續用套筒的外筒與內筒的連接構造與第1貫施方式 -21 - (18) 200404603 的微粒化裝置1 2不同。其他的微粒化裝置1 1 〇的構成， 係與第1實施方式的微粒化裝置1 2的構成相同。此外， 選用與第1實施方式相同的構成之元件則給予相同的符號A gasket 27 is provided at the other end (+ X side) of the inner cylinder 26 of the main sleeve 17, and the inner cylinder 26 is inserted into the recess 37 of the first disc 31 and the second disc 32. The recesses 39 and 19 are integrally fixed to the inside of the outer tube 25. With this structure, the inner cylinder 26 is not only affected by the external pressure of the cylinder 16 acting on the outer cylinder 25, but also forms a closed hollow chamber 20 that does not leak the processing liquid of the raw materials. The hollow chamber 20 is connected to the axial direction passage 22 via a plurality of holes 21. In addition, since the gasket 27 is provided near the connection portion (seat surface 28) of the axial direction passage 22 and the outlet portion 23, the raw material processing liquid does not leak. The outer tube 25 and the inner tube 26 of the sleeve 18a for the first connection will be described with reference to Figs. 5, 9 and 10. In the first splicing sleeve 18a, in order to be able to close both ends of the outer cylinder 25, the first disc 31 and the third disc 33 are locked at both ends. In detail, the outer tube 2 is closed by screwing screw portions provided on the side surfaces of the first circular plate 31 and the second circular plate 32, and screw holes provided on the inner surface of both ends of the outer tube 25, respectively. 5 ends. Of the two circular plates, one circular plate may be directly welded to the inner surface of the end portion of the outer cylinder 25, and the other circular plate may be directly screwed to the inner surface of the end portion of the outer cylinder 25. A concave portion 37 is formed on one end surface of the first circular plate 3 1 of the first connection sleeve 18 a in the same manner as the first circular plate 31 of the main sleeve 17. At the same time, an exit portion 23 is provided along the X axis in the first circular plate 31. The other end face (+ X side) of the third disc 33 of the first splicing sleeve 18a is located on the other end face (+ X side) of the first splicing sleeve 18a, as shown in FIG. 10, to accommodate one end of the inner tube 26 of the first splicing sleeve 18a (-X Side), a recess having a predetermined depth having the same diameter as the inner tube 26 is formed. The center portion of the third disc 33 is located along the X axis and has an exit portion 23 (supply portion) extending from the main sleeve 17. In addition, this part is called the supply department. A groove portion 34 is formed on the seat surface 29 of the recessed portion 38 of the third disc 33, and extends along the Y axis. The other end (+ X side) of the outlet portion 2 3 extending from the main sleeve 17 opens toward the groove portion 34. At the same time, the upper and lower end portions of the groove portion 34 communicate with the through-hole 35 formed along the X axis to the groove portion 34. The groove portion 34 and the through hole 35 constitute a communication path 24. On the other end (+ X side) of the inner tube 26 of the first connection sleeve 1 8 a -16- 299 (13) (13) 200404603, a seal 27 is provided, and the inner tube 26 is inserted in the first The recessed portion 37 of the first circular plate 31 and the recessed portion 38 of the third circular plate 33 are integrally fixed inside the outer tube 25. With this structure, the inner cylinder 26 not only is not affected by the external pressure of the cylinder 16 acting on the outer cylinder 25, but also forms a sealed hollow chamber 20 which does not leak the processing liquid of the raw material. In addition, since the gasket 27 is provided around the connection portion between the axial direction passage 22 and the outlet portion 23, the raw material processing liquid does not leak. The main sleeve 17 and the first splicing sleeve 18 a configured as described above are formed by facing the first circular plate 31 of the main sleeve 17 toward the third circle of the first splicing sleeve 1 8 a. The plates 3 3 are connected to each other. In addition, in order to connect the main sleeve 17 and the first splicing sleeve 18a at the correct positions, a receiving groove 40 for accommodating a protrusion is provided in the first circular plate 31 and the third circular plate 33 (see also Figure 8). With this structure, the main sleeve 17 and the first splicing sleeve 18a can be easily connected. The second connection sleeve 18b and the third connection sleeve 18c, the outer tube 25 and the inner tube 26 are the same as those used in the first connection sleeve 18a as shown in Figs. 6 and 7. Constructed to connect together. At the same time, the first connection sleeve 18a and the second connection sleeve 18b face the third circle of the first connection plate 18a toward the third circle of the second connection sleeve 18b. The plates 33 are connected to each other. In addition, in order to be able to connect the first connection sleeve 18 a and the second connection sleeve 18 b at the correct positions, the first groove and the third circle are provided with receiving grooves 40 for receiving the protrusions ( (Refer to Fig. 8) ° With this structure, it is possible to easily connect the first sleeve 1 8 a for drawing and the sleeve 2 for the table 2 • 17- (14) (14) 200404603 1 8b 〇 The second splicing sleeve 18b and the third splicing sleeve 18.c are formed by facing the first circular plate 31 of the first splicing sleeve 18b to the third circle of the third splicing sleeve 18c. The plates 33 are connected to each other. In addition, in order to be able to connect the second connection sleeve 18b and the third connection sleeve 18c at the correct positions, the first groove and the third circle are provided with a receiving groove 40 for receiving the protrusion (please, (See Figure 8). With this structure, it is possible to easily connect the second connection sleeve 18b and the third connection sleeve 18c. Further, by connecting the main sleeve 17 to the suction port 14, the connection main sleeve 1 is formed. 7 到 管 1 6。 7 to the cylinder 1 6. The third connection sleeve 18c is connected to the discharge port 15 to form the third connection sleeve 18c to the cover 30. The hole diameters of the plurality of hole portions 21 in each sleeve are set to decrease in the + X direction as the number of sleeves is increased. This is because a shock wave in accordance with the particle size of the substance in the raw material is generated inside the hole portion 21. At the same time, it is also possible to make all the hole diameters of the plurality of hole portions 21 in each sleeve according to the requirements. Furthermore, it is possible to arbitrarily change the diameters of the plurality of hole portions 21 in one sleeve. Thereby, a particle size distribution having a plurality of peaks can be obtained. In the first embodiment, the number of splicing sleeves is three, but the number can be changed in accordance with the desired processing amount and particle size distribution. For example, as shown in FIG. 11, in the case where the number of connection sleeves is two, after removing the cover 30 from the cylinder 16, only the V-th connection sleeve 18c is replaced at the center. Only the outlet section 46-18 • 301 (15) (15) 200404603 can be used as the connecting sleeve 47. When increasing the number of splicing sleeves, just insert the desired number of newly-set splicing sleeves between the cylinder 1.6 and the cover 30. ·-The first embodiment is, as shown in FIG. 10, a groove portion 34 formed on the seat surface 29 of the concave portion 38 of the third circular plate 3 3 along the Y axis. However, the arrangement of the 'groove portions 34 is not limited to this, and as shown in Fig. 12', a plurality of groove portions 34 may be formed to extend radially around the opening surface of the outlet portion 23 as a center. In this case, the both end portions of the groove portion 34 communicate with the through-holes 35 formed along the X axis to the respective groove portions 34. Thereby, the raw material can be efficiently sent to the adjacent sleeve. In the first embodiment, as shown in FIG. 10, the through-holes 35 are formed through the recessed portions 38. However, the arrangement of the through holes 35 is not limited to this. As shown in FIG. 13, a part of the side surface of the recessed portion 38 may be removed to form the through holes 35. In the first embodiment, as shown in FIGS. 5 to 7, the main sleeve 17 is locked to both ends of the first circular plate 3 1 and the second circular plate 32 to the outer tube 25, and The first splicing sleeve 18a, the second splicing sleeve 18b, and the third splicing sleeve 18c are locked in the first circular plate 31 and the third circular plate 33 to both ends of the outer tube 25. However, the method of closing both ends of the outer cylinder of each sleeve is not limited to this, and the method shown in FIG. 14 may be formed. In other words, after removing the outer surfaces of the both ends of the outer tube 25, the first circular plate 121, the second circular plate 122, and the third circular plate 123 are formed into a bag shape while a screw portion is provided on the outer surface of the recess. In addition, a screw hole is provided on the inner surface of the screw portion facing the outer tube 25. Next, both ends of the outer tube 25 are closed by screwing the -19- (16) (16) 200404603 screw portion of the outer tube 25 with the screw holes of each circular plate. In this way, "while both ends of the outer tube 25 can be reliably sealed", the circular plates can be easily detached from the outer tube 25. (Second Embodiment) The micronization device 7 of the second embodiment is different from the micronization device 12 of the first embodiment in that the groove portion is formed as shown in Fig. 15. The structure of the other micronization device 70 is the same as that of the micro-nano particle sizer 12 of the first embodiment. In addition, components having the same configuration as those in the first embodiment are given the same reference numerals. In the first embodiment, the groove portion 34 'is formed on the seat surface 29 of the recessed portion 38 provided on the other end surface (+ X side) of the third circular plate 33. In the second embodiment, the groove portion 52 is formed on an end surface (-X side) of one end provided on the third circular plate 33. The both ends of the groove portion 52 communicate with a through hole 54 formed along the X axis. A communication path 50 is formed by the groove portion 52 and the through hole 54. The third circular plate 33 is repaired, and the end surface on the inner tube 26 side (-X side) is not accommodated. The groove portion 5 2 is formed so that the raw material sent from the outlet portion 2 3 does not directly hit the inner tube 26. For this reason, the fixing of the outer tube 25 and the inner tube 26 becomes very stable. At the same time, as shown in Fig. 16, if the suction port 60 is provided at one end of the cylinder 16, all the configurations can be made the same. Therefore, it is possible to more easily manufacture the microparticle device. In addition to the modification examples described above, the modification examples described in the first embodiment -20-383 (17) (17) 200404603 can also be applied to the micronization device 70 of the second embodiment. (Third Embodiment) The micronization device 90 of the third embodiment is different from the micronization device 12 of the first embodiment as shown in Fig. 17 in that a groove portion is formed. The structure of the other micronizing device is the same as that of the micronizing device 12 of the first embodiment. In addition, components having the same configuration as those of the first embodiment are given the same reference numerals. In the first embodiment, the 'groove portion 34 is formed on the seating surface 29 of the recessed portion 38 provided on the other end surface (+ X side) of the third circular plate 33. In the third embodiment, the groove portion 8 2 'is formed on the other end surface (+ X side) of the first circular plate 31 of the sleeve adjacent to the -X side. At both ends of the groove portion 82, a through-hole 84 is formed in communication with the third circular plate of the connection sleeve adjacent to the + X side. A communication path 80 is formed by the groove portion 82 and the through hole 84. The grooves 8 2 are formed by the sleeve 1 and the disc 1 adjacent to the -X side, so that the raw material sent from the outlet portion 2 3 does not hit the inner tube 26 directly. The outer tube 25 and The fixing of the inner tube 26 becomes very stable. The modification described in the first embodiment can be applied to the micronizing device 90 of the third embodiment. (Fourth Embodiment) As shown in FIG. 18, the micronization device 1 10 of the fourth embodiment is the connection structure between the outer tube and the inner tube of each connection sleeve and the first embodiment -21- (18) 200404603 The micronization device 12 is different. The structure of the other micronizing device 1 10 is the same as that of the micronizing device 12 of the first embodiment. In addition, components having the same configuration as those in the first embodiment are given the same reference numerals.

在於第4實施方式中，主套筒17、第1接續用套筒 18a 、及第2接續用套筒1 8 b的第1圓板3 1的構成，係 如下所述。在於第1圓板3 1的一端端面（-X側），爲了收 容各套筒的內筒26(或108)的另一端（+ X側），形成與內筒 2 6(或10 8)的直徑相同之凹陷一定深度的端面之凹部i 12 。在於第1圓板3 1的另一端端面（+ X側），爲了收容在+ X 側鄰接的套筒的內筒1 〇 8的一端（-X側），形成與內筒1 〇 8 相同直徑之凹陷一定深度的凹部11 4。此外，在於第3接 續用套筒18c的第1圓板31，只有形成凹部112。In the fourth embodiment, the configuration of the first disc 31 of the main sleeve 17, the first splicing sleeve 18a, and the second splicing sleeve 18b is as follows. It is located on one end surface (-X side) of the first circular plate 31, and in order to receive the other end (+ X side) of the inner tube 26 (or 108) of each sleeve, it is formed with the inner tube 26 (or 108). The recess i 12 of the end surface of the same diameter recessed to a certain depth. The other end face (+ X side) of the first circular plate 31 is formed to have the same diameter as that of the inner tube 108 in order to receive one end (−X side) of the inner tube 1 08 of the sleeve adjacent to the + X side. The depressions 11 4 are recessed to a certain depth. The first circular plate 31 in the third connection sleeve 18c has only the recessed portion 112 formed.

在於第1接續用套筒18a、第2接續用套筒Ub、及 第3接續用套筒1 8 c的第3圓板3 3的中央部，如第1 8圖 所示，爲了貫通本身內筒1〇8，形成與內筒108相同直徑 之內筒貫通孔1 1 6。 各接續用套筒的內筒1 〇 8，介隔著第3圓板3 3的內 筒貫通孔1 1 6，被插入到本身的接續用套筒的第1圓板3 i 的凹部1 1 2 ;與-X側所鄰接的套筒的第1圓板3 1的凹部 1 1 4之間後，一體式地被固定在外筒2 5的內部。 進一步，溝槽部1 02，係在於—X側所鄰接的套筒的 第1圓板3 1之另一端端面的凹部1 14的中央部，沿著γ 軸被形成。在於溝槽部1 02的兩端部，連通沿著X軸所The central portion of the third circular plate 3 3 of the first connection sleeve 18 a, the second connection sleeve Ub, and the third connection sleeve 1 8 c is shown in FIG. 18 in order to penetrate through itself. The inner tube 108 is formed with an inner tube through-hole 1 16 having the same diameter as the inner tube 108. The inner tube 1 08 of each of the splicing sleeves is inserted into the recess 1 1 of the first disc 3 i of the splicing sleeve through the inner tube penetrating holes 1 1 6 of the third disc 3 3. 2; Between the recesses 1 1 4 of the first circular plate 31 of the sleeve adjacent to the -X side, it is integrally fixed inside the outer tube 25. Further, the groove portion 102 is formed at a central portion of the recessed portion 14 of the other end surface of the first disc 31 adjacent to the -X side of the sleeve, and is formed along the γ axis. It is located at both ends of the groove portion 102, and communicates with each other along the X axis.

-22- (19) 200404603 形成的貫通孔104。進~步，，在於第3圓板33的內筒貫 通孔116的上下部，延伸設置形成相對向的第1圓板31 的貫通孔1 〇 4。藉’由溝槽部1 〇 2與貫通孔1 0 4構成連通路 100 〇 藉由這種構造，各接續用套筒的內筒108的一端端部 ，係被保持在第3圓板3 3的內筒貫通孔1 1 6的緣故，形 成內筒108在外筒25的內部會被固定得更安定。-22- (19) 200404603 formed through hole 104. Further, in the upper and lower portions of the inner cylinder penetrating through hole 116 of the third disc 33, a through hole 104 is formed to extend to form the first disc 31 facing to the opposite side. The communication path 100 is constituted by the groove portion 102 and the through hole 104. With this structure, one end portion of the inner tube 108 of each of the connection sleeves is held on the third disc 3 3 Because of the inner cylinder through-holes 1 1 6, the inner cylinder 108 formed in the outer cylinder 25 will be fixed more securely.

此外，能夠將第1實施方式中說明過的變形例適用在 第4實施方式的微粒化裝置110上。 (實施例）The modification described in the first embodiment can be applied to the micronization device 110 of the fourth embodiment. (Example)

接著，佐以第1 9圖及第20圖說明使用在第1實施方 式的各套筒內的主要部品的汽缸型陶瓷噴嘴，換句話說， 說明內筒26的製造尺寸例。內筒26的胴體直徑D爲15 至25mm，胴體長度爲20至35mm。在於此一胴體內，沿 著內筒26的軸方向，分別朝內筒26的直徑方向穿設8支 孔部2 1。8支孔部21係相互貫穿胴體呈交差狀’且朝相 同方向穿設的4支孔部2 1，係以3至5 m m (P)間隔被配置 在鄰接的孔部21與內筒26的軸方向。進一步’相互被穿 設成交差狀的2支孔部21，係以P/2偏移2支孔部21的 間隔的緣故，相互間不會碰觸。內筒2 6的中空部之軸方 向通路2 2的直徑爲5 m m且連接到8條所有孔部2 1。此 外，將軸方向通路2 2的密封部的厚度F做成5至1 5 mm 。因應需求準備8條孔徑0 · 5 m m的孔部2 1之內筒2 6 ;與 -23- (20) (20)200404603 8條孔徑0 · 3 mm的孔部2 1之內筒2 6等兩種。 組入分別擁有由這種尺寸所構成的內筒26的主套筒 17、第1接續用套筒18a、第2接續用套筒18b、及第3 接續用套筒1 8 c的微粒化裝置1 2，係擁有下列的用途範 例。 · 如第2 1圖所示，依照下列步驟，處理汽車引擎油等 的廢油（物質）來當做品質良好的燃料。首先，加10至50 %重量的水到廢油來製作原料（步驟S 1 )。其次，流入做爲 原料的廢油及水的混合體到微粒化處理系統的原料供給口 1 0 (步驟S 2 )後，利用高壓泵浦1 1加壓原料後送到微粒化 裝置12的吸入口 14 (步驟S3)。接著，使用主套筒17，並 將原料的粒度做成20μιη(步驟S4)後，使用第1接續用套 筒1 8 a，將原料的粒度做成1 μ m (步驟S 5 )，並且使用第2 接續用套筒18b後，將原料的粒度做成5 00nm(步驟S6)， 最後’使用第3接續用套筒1 8 c，將原料的粒度做成 100nm以下（步驟S7)。藉由這一連串的處理，使廢油與水 屬於分子的狀態下混合乳化後，從微粒化裝置1 2的吐出 口 1 5取出被微粒化的原料，然後收容到承接器i 3 (步驟 S8) ° 依據這種步驟，處理該丟棄的各式各樣的廢油後，改 變成品質良好的燃料，換句話說對應各燃燒器具、裝置之 所期望的燃燒。因此，從省能源及環保的觀點來看，對本 發明的微粒化裝置1 2的使用上非常有益處。 此外，本發明的微粒化裝置1 2，係除了處理廢油後 -24- (21) (21)200404603 改變成品質良好的燃料外，在於藥品·輸送系統上，也能 夠使用在將兼備藥品儲存與輸送的微脂體（liposome)加 工成所期望的尺寸的場合。 [產業上的利用] 本發明，係提供一種多樣化、汎用性、簡單化、及製 作性的觀點上佳的物質之微粒化裝置。同時，使用本發明 的微粒化裝置來處理被廢棄的廢油，能夠改變成所期望的 燃料，對於省能源及環保的觀點上有其特別的益處。 【圖式簡單說明】 第1圖，係包含本發明的物質之微粒化裝置的微粒化 處理系統的整體圖。 第2圖，係第1實施方式的物質之微粒化裝置的縱向 斷面圖。 第3圖，係第1實施方式的物質之微粒化裝置的左側 端面圖。 第4圖，係第1實施方式的物質之微粒化裝置的右側 端面圖。 第5圖，係第2圖所示之主套筒及第1接續用套筒的 縱向斷面圖。 第6圖，係第2圖所示之第1接續用套筒及第2接續 用套筒的縱向斷面圖。 第7圖，係第2圖所示之第2接續用套筒及第3接續 -25- (22) 200404603 用套筒的縱向斷面圖。 第.8圖，係由沿著第5圖的I - I線段、第6圖的Π -Π線段或第7圖的m -瓜線段所形成之第1接續用套筒的 橫向斷面圖。 第9圖，係從主套筒側看到的第5圖所示之主套筒的 第1圓板的立體圖。 第1 〇圖’從接續用套筒側看到的第5圖所示之第1 接續用套筒的第2圓板之立體圖。 第1 1圖’係表示第1實施方式的第1變形例的圖形 第1 2圖’係表示第丨實施方式的第2變形例的圖形 〇 第1 3圖’係表示第1實施方式的第3變形例的圖形 〇 第1 4圖’係表示第1實施方式的第4變形例的圖形Next, a cylinder-type ceramic nozzle used as a main part in each sleeve of the first embodiment will be described with reference to FIGS. 19 and 20, and in other words, an example of a manufacturing size of the inner cylinder 26 will be described. The carcass diameter D of the inner tube 26 is 15 to 25 mm, and the carcass length is 20 to 35 mm. Inside this carcass, along the axis of the inner tube 26, 8 holes 21 are formed in the diameter direction of the inner tube 26. The 8 holes 21 intersect the carcass and intersect each other, and pass in the same direction. The four holes 21 provided are arranged at intervals of 3 to 5 mm (P) in the axial direction of the adjacent holes 21 and the inner tube 26. Further, the two hole portions 21 having a difference in shape are passed through each other, and the distance between the two hole portions 21 is shifted by P / 2, so that they do not touch each other. The axial direction passage 2 2 of the hollow portion of the inner tube 26 is 5 mm in diameter and is connected to all eight hole portions 21. In addition, the thickness F of the seal portion of the axial direction passage 22 is made 5 to 15 mm. According to requirements, prepare 8 inner tube 2 6 with hole diameter 0 · 5 mm; and -23- (20) (20) 200404603 8 inner tube 2 with hole diameter 0 · 3 mm 2 6 etc. Both. A micronization device incorporating a main sleeve 17, a first connection sleeve 18a, a second connection sleeve 18b, and a third connection sleeve 18c, each of which has an inner tube 26 composed of such a size. 1 2. It has the following usage examples. · As shown in Figure 21, follow the steps below to dispose of used oil (substances) such as automobile engine oil as a good quality fuel. First, 10 to 50% by weight of water is added to waste oil to make raw materials (step S 1). Next, the mixture of the waste oil and water flowing into the raw material is fed to the raw material supply port 10 of the micronization processing system (step S 2), and then the raw material is pressurized by a high-pressure pump 11 and sent to the micronization device 12 for inhalation. Port 14 (step S3). Next, the main sleeve 17 is used, and the particle size of the raw material is 20 μm (step S4), and then the first splicing sleeve 18a is used to make the particle size of the raw material 1 μm (step S5). After the second splicing sleeve 18b, the particle size of the raw material is set to 500 nm (step S6), and finally, using the third splicing sleeve 18c, the particle size of the raw material is set to 100 nm or less (step S7). After this series of processes, the waste oil and water are mixed and emulsified in a state where the molecules are molecules, and the raw materials that have been micronized are taken out from the outlet 15 of the micronization device 12 and then stored in the receiver i 3 (step S8). ° According to this procedure, after the various waste oils that have been discarded are processed, they are changed into fuels of good quality, in other words, corresponding to the desired combustion of each burning appliance and device. Therefore, from the viewpoint of energy saving and environmental protection, it is very useful for the use of the micronizing device 12 of the present invention. In addition, the micronization device 12 of the present invention can be used in medicine and delivery systems for storage of medicines, in addition to -24- (21) (21) 200404603, which can be used to store both medicines after processing waste oil. When the liposome is processed into the desired size. [Industrial use] The present invention is to provide a micronization device for substances that are excellent in terms of diversification, versatility, simplification, and manufacturability. At the same time, the use of the micronization device of the present invention to treat discarded waste oil can be changed to a desired fuel, which is particularly advantageous from the viewpoint of energy saving and environmental protection. [Brief description of the drawings] Fig. 1 is an overall view of a micronization processing system of a micronization device including a substance of the present invention. Fig. 2 is a longitudinal cross-sectional view of a substance atomizing device according to the first embodiment. Fig. 3 is a left end view of the substance atomizing device of the first embodiment. Fig. 4 is a right end view of the device for atomizing a substance according to the first embodiment. Fig. 5 is a longitudinal sectional view of the main sleeve and the first splicing sleeve shown in Fig. 2; Fig. 6 is a longitudinal sectional view of the first splicing sleeve and the second splicing sleeve shown in Fig. 2. Fig. 7 is a longitudinal sectional view of a second splicing sleeve and a third splicing sleeve shown in Fig. -25- (22) 200404603. Fig. 8 is a cross-sectional view of the first splicing sleeve formed by the line I-I in Fig. 5, the line Π-Π in Fig. 6 or the line m-melon in Fig. 7. Fig. 9 is a perspective view of the first disc of the main sleeve shown in Fig. 5 as viewed from the main sleeve side. Fig. 10 'is a perspective view of the second disc of the first splicing sleeve shown in Fig. 5 when viewed from the splicing sleeve side. FIG. 11 is a diagram showing a first modification of the first embodiment. FIG. 12 is a diagram showing a second modification of the first embodiment. FIG. 13 is a diagram showing a first modification of the first embodiment. 3 Figures of Modifications. FIG. 14 is a figure showing a fourth modification of the first embodiment.

〇 第15圖’係第2實施方式的物質之微粒化裝置的縱 向斷面圖。 第1 6圖’係表示第2實施方式的物質之微粒化裝置 的變形例的圖形。 第1 7 Η ’係第3實施方式的物質之微粒化裝置的縱 向斷面圖。 胃1 8 Η ’係第4實施方式的物質之微粒化裝置的縱 向斷面圖。 -26- (23) 200404603 第1 9圖，係第1實施方式所使用的內筒之縱向斷面 圖。 第2 0圖，係第1實施方式所使用的內筒之立體圖。 第2 1圖，係表示本發明的物質之微粒化裝置的使用 例之流程圖。 主要元件對照表 10 原 料 供 給 □ 11 高 壓 泵 浦 12， 70 ， 90 ， 110 微 业丄 化 裝 置 13 承 接 器 14， 60 吸 入 □ 15 吐 出 □ 16 筒 部 17 主 套 筒 18a 第 1 接 續 用 套 筒 18b 第 2 接 續 用 套 筒 18c 第 3 接 續 用 套 筒 30 蓋 子 19 入 □ 部 20 中 空 室 2 1 多 數 個 孔 部 22 軸 方 向 通 路 23， 46 出 □ 部○ Fig. 15 'is a vertical cross-sectional view of a substance atomizing device according to the second embodiment. Fig. 16 'is a diagram showing a modification example of the substance atomizing device according to the second embodiment. The 17th VII 'is a longitudinal cross-sectional view of a micronizing device for a substance according to the third embodiment. Stomach 18 8 'is a longitudinal sectional view of a micronizing device for a substance according to the fourth embodiment. -26- (23) 200404603 Figure 19 is a longitudinal sectional view of an inner cylinder used in the first embodiment. Fig. 20 is a perspective view of an inner cylinder used in the first embodiment. Fig. 21 is a flowchart showing an example of use of the micronizing device for the substance of the present invention. Comparison table of main components 10 Raw material supply □ 11 High-pressure pump 12, 70, 90, 110 Micro-industrialization device 13 Adapter 14, 60 Suction □ 15 Discharge □ 16 Tube 17 Main sleeve 18a First connection sleeve 18b 2nd splicing sleeve 18c 3rd splicing sleeve 30 cover 19 inlet □ part 20 hollow chamber 2 1 multiple holes 22 axial direction passage 23, 46 outlet □ part

-27- (24) 200404603 (24)-27- (24) 200404603 (24)

25 外 筒 26， 108 內 筒 24， 50 ， 80 ， 100 連 通 路 3 1， 12 1 第 1 圓 板 32， 122 第 2 圓 板 33， 123 第 3 圓 板 34， 52 ， 82 ， 102 溝 槽 部 35， 104 貫 通 部 40 收 容 溝 槽 47 接 續 套 筒 116 內 筒 -eg- 通孔25 Outer cylinder 26, 108 Inner cylinder 24, 50, 80, 100 Communication path 3 1, 12 1 First disc 32, 122 Second disc 33, 123 Third disc 34, 52, 82, 102 Groove section 35, 104 Penetration 40 Receiving groove 47 Connection sleeve 116 Inner tube -eg- Through hole

3ii -28-3ii -28-

Claims (1)

(1) (1)200404603 拾、申請專利範圍 1 . 一種物質之微粒化裝置，係屬於將加壓後送入之 原料予以微粒化之物質微粒化裝置，其特徵爲具備： 戈寸閉一 而將另一端開口的筒體； 及爲了封閉前述筒體的另一端而被螺鎖入前述另一端 的蓋部； 及爲了引導前述原料到裝置內部而設置在前述筒體的 吸入部； Φ 及在於前述筒體的內部，被連接到前述吸入口部後， 因應被設置在內部的孔徑之噴嘴特性來微粒化前述原料的 主套筒； 及在於前述筒體內部，將被依序並列設置，且因應設 置在內部的孔徑之噴嘴特性，進一步地微粒化主套筒內被 微粒化的原料之多數個接續用套筒； 及爲了排出前述多數個接續用套筒微粒化的原料到裝 置外部而設置在前述蓋部的中央部之吐出部。 · 2 ·如申請專利範圍第1項 之物質之微粒化裝置， 其中前述主套筒，係具備： 外筒； 及封閉擁有沿著軸方向形成後將兩端開口的出口部之 前述外筒的一端的第1圓板； 及封閉前述外筒的另一端用的第2圓板； 及夾在封閉一端後在前述出口部的一端打開另一端之 前述第1圓板與第2圓板之間且被固定在前述外筒的內部(1) (1) 200404603 Scope of application and patent application 1. A substance micronization device is a substance micronization device that atomizes the raw materials sent under pressure, and is characterized by: A cylinder with the other end open; and a cap portion that is screwed into the other end to close the other end of the cylinder; and a suction portion provided in the cylinder to guide the material to the inside of the device; and After the inside of the cylinder is connected to the suction port, the main sleeve of the raw material is micronized according to the nozzle characteristics of the aperture provided in the inside; and the inside of the cylinder is arranged side by side in sequence, and In accordance with the characteristics of the nozzles provided in the internal hole, a large number of splicing sleeves for the raw material being micronized in the main sleeve are further atomized; A discharge portion in a central portion of the cover portion. · 2 · The micronization device of the substance in the scope of patent application item 1, wherein the main sleeve is provided with: an outer cylinder; and the outer cylinder which closes the outer cylinder having an exit portion opened at both ends after being formed along the axial direction is provided. A first circular plate at one end; and a second circular plate for closing the other end of the outer cylinder; and between the first circular plate and the second circular plate that are opened at one end of the exit portion after being closed at one end And fixed inside the outer cylinder -29- (2)200404603 之內筒， 在於前述內筒與前述外筒之間形成中空室 入口部的端部在前述中空部開口， 在於前述內筒的側面，於前述中空室將一 且沿著前述內筒的直徑方向形成在前述內筒的 一端開口之多數個前述孔。 3 ·如申請專利範圍第1項之微粒化裝置， 續用套筒具備： 外筒； 及封閉擁有沿著軸方向形成後將兩端開口 前述外筒的一端的第1圓板； 及封閉擁有沿著軸方向形成後將兩端開口 前述外筒的另一端的第3圓板； 及夾在封閉一端後在前述出口部的一端打 前述第1圓板與第3圓板之間且被固定在前述 之內同’ 在於前述內筒與前述外筒之間形成中空室 通路的一端在前述中空部開口， 在於前述內筒的側面，於前述中空室將一 且沿著前述內筒的直徑方向形成在前述內筒的 一端開口之多數個前述孔。 4.如申請專利範圍第2項所記載之物質 置，其中爲了在於對向前述第2圓板的前述第 端端面，收容前述內筒的一端，形成凹陷與前 後，前述吸 / 端開口，並 中空部將另 其中前述接 的出口部之 的連通路之 開另一端之 外筒的內部 後，前述連 端開口，並 中空部將另 之微粒化裝 1圓板的一 述內筒相同-29- (2) 200404603 inner cylinder, the end of the hollow chamber entrance formed between the inner cylinder and the outer cylinder is opened at the hollow portion, and is at the side of the inner cylinder. A plurality of holes are formed at one end of the inner tube so as to face the diameter direction of the inner tube. 3. If the micronization device of the scope of patent application No. 1, the continuous sleeve is provided with: an outer cylinder; and a first disc closed to have one end of the outer cylinder opened at both ends after being formed along the axial direction; A third circular plate having two ends opened to the other end of the outer cylinder after being formed along the axial direction; and sandwiched between the closed end, the first circular plate and the third circular plate are fixed between one end of the outlet portion and fixed. It is the same as in the foregoing, that is, one end forming a hollow chamber passageway between the inner cylinder and the outer cylinder is opened at the hollow portion, is at the side of the inner cylinder, and the hollow chamber will be one along the diameter direction of the inner cylinder. A plurality of holes are formed in one end of the inner tube. 4. The material as described in item 2 of the scope of the patent application, wherein in order to face the first end face of the second disc, the one end of the inner cylinder is accommodated to form a depression and a front and rear, and the suction / end opening is formed, and The hollow part will open the inside of the outer tube at the other end of the communication path of the outlet part connected to the other part, the aforementioned connecting end will be opened, and the hollow part will be the same as the inner tube of the other particle. -30- (3) 200404603 直徑之規定深度的第1凹部， 爲了在於對向前述第1圓板的前述第2圓板的一端端 面，收容前述內筒的另一端，形成凹陷與前述內筒相同直 徑之規定深度的第2凹部。-30- (3) 200404603 The first recess having a predetermined depth in diameter is formed so as to face the one end surface of the second disc facing the first disc to receive the other end of the inner cylinder and form the same recess as the inner cylinder. A second recess having a predetermined depth of diameter. 5 .如申請專利範圍第3項所記載之物質之微粒化裝 置，其中爲了在於對向前述第3圓板的前述第1圓板的一 端端面，收容前述內筒的一端，形成凹陷與前述內筒相同 直徑之規定深度的第1凹部， 爲了在於對向前述第1圓板的前述第3圓板的一端端 面，收容前述內筒的另一端的緣故，形成凹陷與前述內筒 相同直徑之規定深度的第3凹部。 6 .如申請專利範圍第5項所記載之物質之微粒化裝 置，其中前述連通路，係由： 設置在前述第3凹部的底面之溝槽部；5. The micronization device for a substance as described in item 3 of the scope of the patent application, wherein in order to face one end face of the first disc facing the third disc, the one end of the inner cylinder is accommodated to form a depression and the inner portion. The first recess having a predetermined depth of the same diameter of the cylinder is formed so as to face the one end surface of the third disc facing the first disc and accommodate the other end of the inner cylinder, so as to form a recess with the same diameter as the inner cylinder. 3rd recess of depth. 6. The micronization device for a substance as described in item 5 of the scope of the patent application, wherein the communication path is formed by: a groove portion provided on a bottom surface of the third concave portion; 及在於相鄰接的套筒之前述第1圓板的出口部之另一 端將一端開口，且在於前述溝槽部將另一端開口的供給部 及在於前述溝槽部將一端開口，且在於前述中空室將 另一端開口之貫通孔所形成。 7 ·如申請專利範圍第6項所記載之物質之微粒化裝 置，其中前述溝槽部，係以前述的供給部之開口部爲中心 ’將前述第3凹部的底面設置成放射狀。 8 ·如申請專利範圍第5項所記載之物質之微粒化裝 置，其中前述連通路，係由： -31 - 314 (4) (4)200404603 對向著相鄰接的套筒之前述第1圓板的出口部之另一 端’且設蘧在前述第3圓板的另一端端面之溝槽部； 及在於前述溝槽部將一端開口，且在於前述中空室將 另一端開□之貫通孔所形成。 9 · &申請專利範圍第4項所記載之物質之微粒化裝 置’其中介隔著由設置在前述第2圓板的一端端面之溝槽 部；及在前述溝槽部將一端開口且在於前述中空室將另一 端開□之貫通孔所形成的連通孔，形成前述吸入口的端部 φ 在前述中空室開口。 1 0 · —種物質之微粒化裝置，係屬於微粒化被加壓後 輸送過來的原料的物質之微粒化裝置，其特徵爲具備： 封閉一端而打開另一端的筒體； 及爲了封閉前述的筒體的另一端而設置在前述筒體的 另一端的蓋部； 及爲了導入前述原料到裝置內部而設置在前述筒體的 吸入口部； 及在於前述筒體的內部’被連接到前述吸入口部後， 因應被設置在內部的孔徑之噴嘴特性來將前述原料微粒化 的主套筒； 及在前述筒體的內部’將被依序並排設置’且因應設 置在內部的孔徑之噴嘴特性，進一步地微粒化前述主套筒 微粒化的原料之多數個接續用套筒·’ 及排出前述多數個接續用套筒微粒化的原料之排出套And the other end of the outlet portion of the first circular plate adjacent to the sleeve is opened at one end, and the supply portion is opened at the groove portion at the other end, and the groove portion is opened at one end, and The hollow chamber is formed by a through hole opened at the other end. 7. The micronization device of the substance described in item 6 of the scope of the patent application, wherein the groove portion is centered on the opening portion of the supply portion ′, and the bottom surface of the third recess portion is provided in a radial shape. 8 · The micronization device of the substance as described in item 5 of the scope of the patent application, wherein the communication path is: -31-314 (4) (4) 200404603 facing the first circle facing the adjacent sleeve A groove portion provided at the other end of the exit portion of the plate and provided on the end surface of the other end of the third circular plate; and a through hole formed by opening one end of the groove portion and opening the other end by the hollow chamber form. 9 & A micronization device for a substance described in item 4 of the scope of the patent application, wherein a groove portion provided on one end surface of the second circular plate is interposed therebetween; In the hollow chamber, a communication hole formed by a through hole having the other end opened to form an end portion φ of the suction port opens in the hollow chamber. 1 0 · — A device for atomizing a substance, which is a device for atomizing a material that is atomized and conveyed after being pressurized, and is characterized in that: it is provided with a cylinder closed at one end and opened at the other end; A cover portion provided at the other end of the cylinder body at the other end of the cylinder body; and a suction port portion provided at the cylinder body for introducing the raw material into the device; and the inside of the cylinder body is connected to the suction After the mouth, the main sleeve that atomizes the raw materials according to the characteristics of the nozzles of the apertures provided inside; and the nozzle characteristics of the nozzles that will be "side-by-side ordered" and corresponding to the diameters of the apertures provided inside the cylinder Further, a plurality of splicing sleeves of the raw material of which the main sleeve is micronized is further atomized, and a discharge sleeve which discharges the plurality of splicing materials of the plurality of splicing sleeves. -32- (5) (5)200404603 及爲了將F前述排出套筒所排出的原料排出到裝置外部 而設置在前述蓋部的中央部之吐出口部。 11 · 一種物質之微.粒化處理方法，係屬於將擁有由入 口部、孔部、及出口部所形成的流體通路之套筒多數並排 設置在擁有吸入口部及吐出口部的筒體的內部後，連接最 先的套筒的入口部到前述吸入口部，並且依序地連接前述 最先的套筒之出口部到下一個套筒的入口部，並連接最後 一個套筒的出口部到前述吐出口部的微粒化裝置，做成處 理廢油來當做燃料的處理方法，其特徵爲： 對廢油加上1 〇至5 0 %重量的水來做成原料後， 利用高壓泵浦將前述原料加壓， 輸送前述被加壓的原料到前述吸入口後， 依序將原料微粒化成對應設置在各套筒的內部之前述 孔部的噴嘴特性的粒度， 並且從前述吐出口將被微粒化成適當的粒度之前述原 料取出來當做乳化燃料。-32- (5) (5) 200404603 and a discharge port provided at a central portion of the cover portion in order to discharge the raw material discharged from the discharge sleeve F to the outside of the apparatus. 11 · A substance micro-granulation treatment method is a method in which a plurality of sleeves having a fluid passage formed by an inlet portion, a hole portion and an outlet portion are arranged side by side in a cylinder having a suction inlet portion and a discharge outlet portion. After inside, connect the inlet of the first sleeve to the suction port, and sequentially connect the outlet of the first sleeve to the inlet of the next sleeve, and connect the outlet of the last sleeve. The micronization device to the aforementioned outlet is made into a method for treating waste oil as fuel, and is characterized by adding 10 to 50% by weight of water to the waste oil to make raw materials, and then using a high-pressure pump After the raw material is pressurized and the pressurized raw material is conveyed to the suction port, the raw material is sequentially micronized into a particle size corresponding to a nozzle characteristic of the hole portion provided in each of the sleeves. The aforementioned raw material which is atomized into an appropriate particle size is taken out as an emulsified fuel. -33--33-
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JP4707342B2 (en) * 2004-07-20 2011-06-22 株式会社東海 Substance atomization equipment
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US20100252481A1 (en) * 2007-10-22 2010-10-07 Mg Grow Up Corp. Reformed fuel oil, process for producing the same and apparatus therefor
JP2010279904A (en) * 2009-06-04 2010-12-16 Tomihisa Naito Atomizing apparatus and atomization system
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