JPH02160033A - Pellet extruder - Google Patents
Pellet extruderInfo
- Publication number
- JPH02160033A JPH02160033A JP63315263A JP31526388A JPH02160033A JP H02160033 A JPH02160033 A JP H02160033A JP 63315263 A JP63315263 A JP 63315263A JP 31526388 A JP31526388 A JP 31526388A JP H02160033 A JPH02160033 A JP H02160033A
- Authority
- JP
- Japan
- Prior art keywords
- screw
- kneading
- pellet
- disk
- die
- Prior art date
- Legal status (The legal status 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 status listed.)
- Granted
Links
- 239000008188 pellet Substances 0.000 title claims abstract description 30
- 238000004898 kneading Methods 0.000 claims abstract description 33
- 239000002994 raw material Substances 0.000 claims abstract description 20
- 230000007246 mechanism Effects 0.000 claims abstract description 18
- 238000001125 extrusion Methods 0.000 claims abstract description 13
- 230000000149 penetrating effect Effects 0.000 claims abstract description 5
- 239000011550 stock solution Substances 0.000 claims description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 2
- 230000032258 transport Effects 0.000 claims 2
- 239000000463 material Substances 0.000 abstract description 10
- 238000013329 compounding Methods 0.000 abstract description 2
- 238000000034 method Methods 0.000 description 7
- 238000002156 mixing Methods 0.000 description 5
- 239000000344 soap Substances 0.000 description 5
- 230000006835 compression Effects 0.000 description 3
- 238000007906 compression Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000011347 resin Substances 0.000 description 2
- 229920005989 resin Polymers 0.000 description 2
- 230000005540 biological transmission Effects 0.000 description 1
- 239000003638 chemical reducing agent Substances 0.000 description 1
- 238000004040 coloring Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 229940079593 drug Drugs 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- -1 foodstuffs Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 238000004080 punching Methods 0.000 description 1
- 238000010008 shearing Methods 0.000 description 1
- 239000007779 soft material Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B30—PRESSES
- B30B—PRESSES IN GENERAL
- B30B11/00—Presses specially adapted for forming shaped articles from material in particulate or plastic state, e.g. briquetting presses, tabletting presses
- B30B11/22—Extrusion presses; Dies therefor
- B30B11/24—Extrusion presses; Dies therefor using screws or worms
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B7/00—Mixing; Kneading
- B29B7/30—Mixing; Kneading continuous, with mechanical mixing or kneading devices
- B29B7/34—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices
- B29B7/38—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary
- B29B7/40—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with single shaft
- B29B7/42—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with single shaft with screw or helix
- B29B7/428—Parts or accessories, e.g. casings, feeding or discharging means
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/001—Combinations of extrusion moulding with other shaping operations
- B29C48/0022—Combinations of extrusion moulding with other shaping operations combined with cutting
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/03—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
- B29C48/04—Particle-shaped
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/03—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
- B29C48/05—Filamentary, e.g. strands
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
- B29C48/362—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using static mixing devices
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
- B29C48/50—Details of extruders
- B29C48/505—Screws
- B29C48/535—Screws with thread pitch varying along the longitudinal axis
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
- B29C48/50—Details of extruders
- B29C48/76—Venting, drying means; Degassing means
- B29C48/761—Venting, drying means; Degassing means the vented material being in liquid form
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/268—Throttling of the flow, e.g. for cooperating with plasticising elements or for degassing
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
- Glanulating (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、主として石けん等の化学材料を混練するとと
もに、所定の大きさのペレット状に押出し成形するよう
にしたペレット押出機に係り、詳しくは原液中の含水率
を低下させる真空タンクから取出された原料を、混練し
ながら搬送するスクリュー装置と、そのスクリュー装置
の搬送終端に押し出し用のダイスとを偵え、がつ、この
ダイスの出口側にカッターを配設してあるベレット押出
機関する。[Detailed Description of the Invention] [Field of Industrial Application] The present invention mainly relates to a pellet extruder for kneading chemical materials such as soap and extruding them into pellets of a predetermined size. A screw device is used to knead and convey raw materials taken out from a vacuum tank to reduce the water content in the raw solution, and an extrusion die is located at the end of the conveyance of the screw device. A pellet extrusion engine with a cutter installed on the side.
従来では、第8図に示すように、原料供給部(2)から
漏下してきた原料を混練しながら搬送するスクリュー装
置(4)、の終端に、多数の貫通小孔を形成したダイス
(11)を備え、かつ、このダイス(11)の反スクリ
ュー側に回転式のカッター(12)を配設して、ダイス
(11)より押し出されてくる材料を所定長さのペレッ
ト状に切断するペレット押出機が知られている。Conventionally, as shown in Figure 8, a die (11 ), and a rotary cutter (12) is arranged on the opposite side of the die (11) to cut the material extruded from the die (11) into pellets of a predetermined length. Extruders are known.
前記従来技術によるペレット押出機は、スクリューで原
料を搬送させることによって均一に混練しながら押し出
し成形を行い、同時に切断加工もできるようにカッター
を配して、所定の大きさのペレット状の材料を形成する
ようにしたものである。The pellet extruder according to the conventional technology performs extrusion molding while uniformly kneading the raw materials by conveying them with a screw, and at the same time, a cutter is arranged so that the material can be cut into pellets of a predetermined size. It was designed so that it could be formed.
材料をベレット状にすれば、例えばサイロ、箱等の容器
に収納する場合に収納し易いものであって、取り扱い性
に優れているものである。If the material is made into a pellet shape, it can be easily stored in a container such as a silo or a box, and has excellent handling properties.
ペレット状の材料は、次工程で着色、賦香、およびその
ための混練等の処理を経てから所定の形状に仕上げるこ
とによって製品化されるのであるが、製品の品質はベレ
ット状のときの配合状態の良し悪しで大きく左右される
。Pellet-shaped materials are made into products by undergoing processes such as coloring, flavoring, and kneading in the next process, and then finishing them into a predetermined shape. A lot depends on how good or bad it is.
そして、最近になって、原料の配合状態を均一化するの
にスクリューによる搬送のみではまだまだネート分であ
ることが判ってきた。つまり、ベレット状の材料に、視
認できる程度の混練ムラが生じたり91.プツ(サンド
フィル)が依然として存在している事実がG(IPJさ
れるようになったのである。Recently, it has been found that conveyance by screws alone is insufficient to even out the blended state of raw materials. In other words, visible kneading unevenness may occur in the pellet-shaped material. The fact that putu (sandfill) still exists has become known as G (IPJ).
そこで、混練不良を改善するために、回転カッターの後
に専用のミキシング装置を付設したり、または、成形加
工されたペレットを再び、混練機で処理するといった具
合に工程を重複させたりすることが試されたが、混練不
良は改善されるものの、その工程が長(なって作業能率
が悪化し、生産性が低いという新たな不具合を解消し得
ないものであった。Therefore, in order to improve the kneading defects, attempts have been made to install a dedicated mixing device after the rotary cutter, or to duplicate the process, such as processing the formed pellets again in the kneading machine. However, although the defective kneading was improved, the process was long (which worsened work efficiency and productivity was low), which were new problems that could not be solved.
本発明は、原料の混練ムラをペレット押出機に1回通す
のみの工程によって極力無くすことにより、均一な配合
状態のベレット軟材料を得られるようにして前記不具合
を回避することを目的とする。The object of the present invention is to avoid the above-mentioned problems by eliminating uneven kneading of raw materials as much as possible by passing the raw materials through a pellet extruder only once, thereby making it possible to obtain a pellet soft material with a uniform blending state.
上記目的を達成するために本発明は、冒頭に記載したペ
レット押出機において、前記スクリュー装置を、前スク
リューと後スクリュー、およびこれら前後スクリュー間
に設けられた混練機構から構成し、前記混練機構は、前
記前スクリューの搬送終端に連結され、この前スクリュ
ーと伴に回転し、かつ、スクリュー軸方向に貫通する複
数の孔が形成された回転ディスク、および、この回転デ
ィスクと前記後スクリューとの間に、スクリュー軸方向
に貫通する複数の孔が形成され、かつ、前記回転ディス
クと対向する状態で固定配置された固定ディスクとから
構成してあることを特徴とする。In order to achieve the above object, the present invention provides the pellet extruder described at the beginning, in which the screw device is composed of a front screw, a rear screw, and a kneading mechanism provided between these front and rear screws, and the kneading mechanism is , a rotating disk connected to the conveying end of the front screw, rotating together with the front screw, and having a plurality of holes penetrating in the axial direction of the screw; and between the rotating disk and the rear screw. It is characterized by comprising a fixed disk having a plurality of holes penetrating in the direction of the screw axis and fixedly disposed opposite to the rotating disk.
そして、前記後スクリューのピッチを、前記前スクリュ
ーのピッチよりも大きくすれば好ましいものである。It is preferable that the pitch of the rear screw is larger than the pitch of the front screw.
また、前記後スクリューを省略するとともに、前記ダイ
スを前記混練機構の搬送下手側近傍に配置するように構
成しても良い。Further, the rear screw may be omitted and the die may be arranged near the downstream side of the conveyance side of the kneading mechanism.
前記構成によれば、前スクリューで搬送されてきた原料
は回転ディスクの複数の孔から分散されて押し出され、
そして、対向する固定ディスクとによって1回転方向の
せん断による練り作用を受けつつ今度は固定ディスクの
複数の孔へ再び強制分散されて後スクリューへと送られ
る。According to the above configuration, the raw material conveyed by the front screw is dispersed and extruded through the plurality of holes of the rotating disk,
Then, while being subjected to the kneading action of shearing in the direction of one rotation by the opposing fixed disk, it is again forcibly dispersed into the plurality of holes of the fixed disk and sent to the rear screw.
そして、後スクリューのピッチを前スクリューのピッチ
より大きくすれば、混練機構の前側の搬送圧と後側の搬
送圧との差を大きくすることができるので、原料が混練
機構をスムーズに通過できるようになる。If the pitch of the rear screw is made larger than the pitch of the front screw, the difference between the conveying pressure on the front side of the kneading mechanism and the conveying pressure on the rear side can be increased, so that the raw materials can pass through the kneading mechanism smoothly. become.
また、後スクリューを無くして固定ディスクとダイス間
距離を狭くして配置すれば、スクリュー装置の全長をそ
の分短くすることができる。Further, if the rear screw is eliminated and the distance between the fixed disk and the die is narrowed, the overall length of the screw device can be shortened accordingly.
従って、請求項1記載のペレット押出機では、スクリュ
ーによる搬送途中で、回転ディスクと固定ディスク、お
よびこれらの協働によって、原料が分散、混練、そして
また分散される作用を受けるとともに、前記混練は原料
の搬送方向に対して直交する方向へのせん断力による強
制混練であるから、この混練機構によって原料は、従来
に比べてその配合状態の均一度が飛曜的に向上し、より
品質の優れたペレット状材料を得ることができるように
なるとともに、これによって他に専′用のミキシング装
置を付設することや、もう−変温練機で処理するといっ
たことが不要となって、作業能率の高い生産性に優れた
ペレット押出機にし得た。Therefore, in the pellet extruder according to the first aspect, the raw material is dispersed, kneaded, and dispersed again by the rotating disk and the fixed disk and their cooperation during transportation by the screw, and the kneading is This kneading mechanism uses shear force in a direction perpendicular to the direction in which the raw materials are transported, so this kneading mechanism dramatically improves the uniformity of the blended state of the raw materials compared to conventional methods, resulting in even better quality. In addition to making it possible to obtain pelletized materials, this also eliminates the need for special mixing equipment or processing with variable temperature kneading machines, improving work efficiency. We were able to create a pellet extruder with excellent productivity.
そして、請求項2記載のペレット押出機では、請求項1
による効果に加え、スクリュー軸方向の違いによって後
スクリューによる搬送速度が前スクリューのそれよりも
大となり、この速度差で原料が混練機構をスムーズに通
過できるので、押出機全体としての作業スピードの向上
に寄与できるとともに、配合状態の均一度をより一層改
善することが可能になる。In the pellet extruder according to claim 2, the pellet extruder according to claim 1
In addition to the effect of In addition, it is possible to further improve the uniformity of the blended state.
また、請求項3.記載のペレット押出機では、優れた配
合状態を得られる混純機構を備えつつ、ペレット押出機
としての小型化が図れ、かつ、それによるコストダウン
も期待できるので、例えば、後スクリューによる作用に
あまり影響されない低粘度原料を対象とする場合等では
、配合状態の均一度を改善しながらもより一層コンバク
で経済的なペレット押出機を実現できる。。Also, claim 3. The described pellet extruder is equipped with a mixing and purifying mechanism that can obtain an excellent compounding state, and it is also possible to downsize the pellet extruder and thereby reduce costs. When using low-viscosity raw materials that are not affected by this, it is possible to realize a pellet extruder that is more compact and economical while improving the uniformity of the blending state. .
(実施例〕
以下に本発明によるペレット押出機の実施例を図面を参
照しながら説明する。(Example) Examples of the pellet extruder according to the present invention will be described below with reference to the drawings.
第4.5図に示すように、ペレット押出機は、駆動部(
1)、原料供給部(2)、および搬送押出部(3)から
成っている。As shown in Figure 4.5, the pellet extruder has a drive section (
1), a raw material supply section (2), and a conveyance extrusion section (3).
前記駆動部(1)は搬送押出部(3)に内装された後述
のスクリュー装置(4)を回転駆動するものであり、モ
ータ(M)、無段変速機(5)、減速機(6)等から構
成されている。The drive unit (1) rotates a screw device (4), which will be described later, which is installed in the conveyance and extrusion unit (3), and includes a motor (M), a continuously variable transmission (5), and a speed reducer (6). It is composed of etc.
第7図に示すように、前記原料供給部(2)は、所定の
割合で混合されて原液タンク(26)から送られてくる
石けん原液を貯留部(23)で−旦貯留し、それから熱
交換器(24)で加熱するという前工程に連続させてあ
り、ポンプ(図外)によって真空に近(減圧され、前記
前工程を経て送られてくる石けん原液を乾燥させる真空
タンク(7)と、この真空タンク(7)下端部と前記搬
送押出部(3)の搬送始端部とを連結する漏下部(8)
とから構成されている。As shown in FIG. 7, the raw material supply section (2) temporarily stores the soap stock solution mixed at a predetermined ratio and sent from the stock solution tank (26) in a storage section (23), and then heats it. A vacuum tank (7) is connected to the pre-process of heating with an exchanger (24), and is reduced to a near vacuum (depressurized) by a pump (not shown), and dries the soap stock solution sent through the pre-process. , a leakage part (8) connecting the lower end of the vacuum tank (7) and the transport start end of the transport extruder (3);
It is composed of.
前記搬送押出部(3)は、練出部(9)とペレット押出
部(lO)から構成されており、次に詳述する。The conveyance extrusion section (3) is composed of a kneading section (9) and a pellet extrusion section (lO), which will be described in detail next.
第1図に示すように、搬送押出部(3)は、漏下部(8
)から供給されてきた石けん原料を搬送するスクリュー
装置(4)の搬送終端に押し出し川のダイス(11)を
備え、かつ、このダイス(11)の後側に回転式のカッ
ター(12)を配設してある。As shown in FIG.
) is equipped with an extrusion die (11) at the end of the conveyance of a screw device (4) that conveys soap raw materials supplied from It has been set up.
前記スクリュー装置(4)は、前スクリュー(13)と
後スクリュー(14)、およびこれら前後スクリュー(
13) 、 (14)間に設けられた混練機構(15)
から構成されている。The screw device (4) includes a front screw (13), a rear screw (14), and these front and rear screws (
13), (14) Kneading mechanism (15) provided between
It consists of
前記混練機構(15)は、第2図にも示すように、前ス
クリュー(13)の搬送終端に連結され、この前スクリ
ュー(13)と一体回転し、かつ、スクリュー軸方向に
貫通する複数の孔が形成された回転ディスク(16)、
および、この回転ディスク(16)と前記後スクリュー
(14)との間に、スクリュー軸方向に、貫通する複数
の孔を形成し、かつ、前記回転ディスク(16)と対向
する状態で固定配置された固定ディスク(17)とから
構成されている。そして、固定ディスク(17)の孔は
、回転ディスク(16)の孔よりも小径としてある。As shown in FIG. 2, the kneading mechanism (15) is connected to the conveying end of the front screw (13), rotates integrally with the front screw (13), and has a plurality of kneading mechanisms that penetrate in the axial direction of the screw. a rotating disk (16) with holes formed therein;
A plurality of holes are formed between the rotating disk (16) and the rear screw (14) in the axial direction of the screw, and the screw is fixedly disposed facing the rotating disk (16). and a fixed disk (17). The holes in the fixed disk (17) have a smaller diameter than the holes in the rotating disk (16).
前スクリュー(13)、後スクリュー(14)、および
、カッター(12)の三者は一体回転するようにキ一連
結され、前スクリュー(13)と回転ディスク(16)
もキ一連結されている。The front screw (13), the rear screw (14), and the cutter (12) are linked together so that they rotate together, and the front screw (13) and the rotating disk (16)
Ki is also connected.
前記固定ディスク(17)は、前スクリュー(13)を
内装する前シリンダ(18)と、後スクリュー(14)
を内装する後シリンダ(19)との連結部によってこれ
らシリンダ(1B) 、 (19)間に挟持嵌合固定さ
れているとともに、樹脂製の軸受(20)を介して前ス
クリュー(13)を回転自在に支持している。The fixed disk (17) includes a front cylinder (18) that houses a front screw (13), and a rear screw (14).
These cylinders (1B) and (19) are clamped and fixed by the connecting part with the rear cylinder (19) which is installed inside, and the front screw (13) is rotated via the resin bearing (20). I freely support it.
前記ダイス(11)は、第3図にも示すように、後シリ
ンダ(19)と、この後シリンダ(19)へ開閉自在に
枢支された蓋体(21)とによって挟持嵌合固定されて
いるとともに、軸受(22)を介して後スクリュー(1
4)を回転自在に支持している。As shown in FIG. 3, the die (11) is clamped and fixed by a rear cylinder (19) and a lid (21) which is pivotally supported to the rear cylinder (19) so as to be openable and closable. At the same time, the rear screw (1) is inserted through the bearing (22).
4) is rotatably supported.
そして、前スクリユー(13)のピッチ(Pl)は、抜
スクリュー(14)のピッチ(P2)よりも小に設定し
てある。The pitch (Pl) of the front screw (13) is set smaller than the pitch (P2) of the extraction screw (14).
尚、図中(23)は、後シリンダ(19)支持用の受は
台であり、(24) 、 (25)はそれぞれ冷却用の
水路である。In the figure, (23) is a support for supporting the rear cylinder (19), and (24) and (25) are water channels for cooling, respectively.
また、第2図における(26)は原料を濾過するメツシ
ュ状のディスク網、(27)は、固定ディスク(17)
の孔よりも小なる孔を多数明けたパンチングプレートで
、前記ディスクm (26)の固定ディスク(17)の
孔部に対する強度補償を行なうものである。In addition, (26) in Fig. 2 is a mesh-like disk network for filtering raw materials, and (27) is a fixed disk (17).
This is a punching plate having a large number of holes smaller than the holes of the disk m (26) to compensate for the strength of the holes in the fixed disk (17).
前記練出部(9)は前シリンダ(18)相当部位、前記
ペレット押出部(10)は後シリンダ相当部位をそれぞ
れ示すものである。The kneading section (9) corresponds to the front cylinder (18), and the pellet extrusion section (10) corresponds to the rear cylinder.
本発明によるベレット押出機は、石けん原料の他、プラ
スチック等の樹脂材料、食料品、薬品等に利用すること
が可能である。The pellet extruder according to the present invention can be used not only for soap raw materials, but also for resin materials such as plastics, foodstuffs, medicines, and the like.
また、前スクリュー(13)、後スクリュー(14)、
およびカッタ、−(12)の回転軸を一体に構成しても
良い。In addition, the front screw (13), the rear screw (14),
The rotary shafts of the cutter and the cutter (12) may be integrally formed.
(別実施例〕
第7図に示すように、前スクリュー(13)後端の混練
機構(15)の固定ディスク(17)の搬送下手側近傍
にダイス(11)が位置するようにしても良い。(Another Embodiment) As shown in FIG. 7, the die (11) may be located near the conveyance side of the fixed disk (17) of the kneading mechanism (15) at the rear end of the front screw (13). .
この場合、後スクリューは無く、代わりに固定ディスク
(17)とダイス(11)間に圧縮室(25)が形成さ
れており、混練機構(15)通過後の原料は、前記圧縮
室(25)で分散および圧縮による混練作用を受けつつ
一旦貯留され、前スクリュー(13)の搬送圧によって
ダイス(11)を通過するのである。In this case, there is no rear screw, and instead a compression chamber (25) is formed between the fixed disk (17) and the die (11), and the raw material after passing through the kneading mechanism (15) is transferred to the compression chamber (25). It is temporarily stored while being subjected to the kneading action of dispersion and compression, and is passed through the die (11) by the conveying pressure of the front screw (13).
尚、特許請求の範囲の項に図面との対照を便利にする為
に符号を記すが、該記入により本発明は添付図面の構造
に限定されるものではない。Incidentally, although reference numerals are written in the claims section for convenient comparison with the drawings, the present invention is not limited to the structure shown in the accompanying drawings.
図面は本発明に係るベレット押出機の実施例を示し、第
1図は搬送押出部の縦断面図、第2図は一部断面要部図
、第3図はペレット押出部の側面図、第4図は全体正面
図、第5図は第4図の側面図、第6図は前工程の概略構
成図、第7図は別実施例による搬送押出部の縦断面図、
第8図は従来例の全体正面図である。
(4)・・・・・・スクリュー装置、(7)・・・・・
・真空タンク、(11)・・・・・・ダイス、 (12
)・・・・・・カッター(13)・・・・・・前スクリ
ュー、 (14)・・・・・・後スクリュー、(15)
・・・・・・混taJIa構、(16)・・・・・・回
転ディスク、(17)・−・・・固定ディスク。The drawings show an embodiment of the pellet extruder according to the present invention, in which FIG. 1 is a longitudinal cross-sectional view of the conveying extrusion section, FIG. 2 is a partial sectional view of the main part, and FIG. 4 is an overall front view, FIG. 5 is a side view of FIG. 4, FIG. 6 is a schematic configuration diagram of the previous process, and FIG. 7 is a longitudinal cross-sectional view of a conveyance extrusion section according to another embodiment.
FIG. 8 is an overall front view of the conventional example. (4)...Screw device, (7)...
・Vacuum tank, (11)... Dice, (12
)...Cutter (13)...Front screw, (14)...Rear screw, (15)
...Mixed taJIa structure, (16) ... Rotating disk, (17) ... Fixed disk.
Claims (1)
取出された原料を、混練しながら搬送するスクリュー装
置(4)と、そのスクリュー装置(4)の搬送終端に押
し出し用のダイス(11)とを備え、かつ、このダイス
(11)の出口側にカッター(12)を配設してあるペ
レット押出機であって、前記スクリュー装置(4)を、
前スクリュー(13)と後スクリュー(14)、および
これら前後スクリュー(13)、(14)間に設けられ
た混練機構(15)から構成し、前記混練機構(15)
は、前記前スクリュー(13)の搬送終端に連結され、
この前スクリュー(13)と伴に回転し、かつ、スクリ
ュー軸方向に貫通する複数の孔が形成された回転ディス
ク(16)、および、この回転ディスク(16)と前記
後スクリュー(14)との間に、スクリュー軸方向に貫
通する複数の孔が形成され、かつ、前記回転ディスク(
16)と対向する状態で固定配置された固定ディスク(
17)とから構成してあるペレット押出機。 2、前記後スクリュー(14)のピッチを、前記前スク
リュー(13)のピッチよりも大きくしてある請求項1
記載のペレット押出機。 3、前記後スクリュー(14)を省略するとともに、前
記ダイス(11)を前記混練機構(15)の搬送下手側
近傍に配置してある請求項1.記載のペレット押出機。[Claims] 1. A screw device (4) that transports the raw material taken out from the vacuum tank (7) to reduce the water content in the stock solution while kneading it, and a screw device (4) at the end of the transport of the screw device (4). A pellet extruder is equipped with an extrusion die (11) and a cutter (12) is disposed on the exit side of the die (11), the screw device (4) comprising:
Consisting of a front screw (13), a rear screw (14), and a kneading mechanism (15) provided between these front and rear screws (13) and (14), the kneading mechanism (15)
is connected to the conveying end of the front screw (13),
A rotating disk (16) that rotates together with the front screw (13) and has a plurality of holes penetrating in the axial direction of the screw, and a connection between the rotating disk (16) and the rear screw (14). A plurality of holes penetrating in the screw axial direction are formed between the rotating disks (
A fixed disk (
17) A pellet extruder comprising: 2. Claim 1, wherein the pitch of the rear screw (14) is larger than the pitch of the front screw (13).
Pellet extruder as described. 3. Claim 1, wherein the rear screw (14) is omitted and the die (11) is arranged near the downstream side of the conveyance side of the kneading mechanism (15). Pellet extruder as described.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63315263A JPH02160033A (en) | 1988-12-13 | 1988-12-13 | Pellet extruder |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63315263A JPH02160033A (en) | 1988-12-13 | 1988-12-13 | Pellet extruder |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH02160033A true JPH02160033A (en) | 1990-06-20 |
| JPH0422613B2 JPH0422613B2 (en) | 1992-04-20 |
Family
ID=18063325
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP63315263A Granted JPH02160033A (en) | 1988-12-13 | 1988-12-13 | Pellet extruder |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH02160033A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| AT13181U1 (en) * | 2012-05-30 | 2013-08-15 | Piwag Entsorger Gmbh | Process for producing fuel pellets |
-
1988
- 1988-12-13 JP JP63315263A patent/JPH02160033A/en active Granted
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| AT13181U1 (en) * | 2012-05-30 | 2013-08-15 | Piwag Entsorger Gmbh | Process for producing fuel pellets |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0422613B2 (en) | 1992-04-20 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US3999921A (en) | Two-channel extruder with mixer | |
| US5589203A (en) | Vacuum kneading and extruding apparatus | |
| JPH0343229A (en) | Extrusion molding machine | |
| US20040094862A1 (en) | Multi-screw extruder and method for treating and/or processing elastomers with added filler | |
| US5421650A (en) | Mixing machinery of the transfermix type | |
| JPH05220803A (en) | Method and device for extrusion molding of powder material | |
| KR20200062426A (en) | Device for manufacturing laver snack | |
| US3025565A (en) | Process and apparatus for granulating and forming plastic masses | |
| US3457880A (en) | Dough molding press | |
| KR900006366A (en) | Continuous manufacturing method of thermally vulcanized silicone rubber compound | |
| JPS61260829A (en) | Apparatus for kneading dough for producing bread or confectionery and decomposing and homogenizing food and feedcomponents at low temperature | |
| EP0189961B1 (en) | Apparatus for compacting powdered and fibrous raw materials to a pellet product | |
| CN110802828A (en) | Double-screw extruder for polyolefin filling masterbatch | |
| US6143811A (en) | Method of producing compound pellets containing wood flour | |
| JPH02160033A (en) | Pellet extruder | |
| US2531739A (en) | Process for preparing thermoplastic material | |
| CN221417375U (en) | Double-screw extrusion device for EPDM sponge production | |
| CN223474940U (en) | A material conveying and mixing device for a granulator | |
| CN221365778U (en) | Plastic extruder that production efficiency is high | |
| JPH067760A (en) | Apparatus for treating organic substance | |
| CN214687384U (en) | Rubber mixing device | |
| CN214636184U (en) | A fertilizer granulation device for organic fertilizer production | |
| CN213533339U (en) | Granulator is used in wear-resisting agent production | |
| CN205467213U (en) | Single screw plastic exdruder | |
| CN116020338B (en) | A twin-screw extruder for biodegradable materials |