JPS62180746A - Reaction device - Google Patents
Reaction deviceInfo
- Publication number
- JPS62180746A JPS62180746A JP61019573A JP1957386A JPS62180746A JP S62180746 A JPS62180746 A JP S62180746A JP 61019573 A JP61019573 A JP 61019573A JP 1957386 A JP1957386 A JP 1957386A JP S62180746 A JPS62180746 A JP S62180746A
- Authority
- JP
- Japan
- Prior art keywords
- temp
- temperature
- outlet
- vessel
- temps
- 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.)
- Pending
Links
- 238000006243 chemical reaction Methods 0.000 title claims abstract description 13
- 238000005192 partition Methods 0.000 claims abstract description 17
- 238000004939 coking Methods 0.000 claims abstract description 14
- 238000003756 stirring Methods 0.000 claims description 21
- 238000001514 detection method Methods 0.000 claims description 11
- 239000000126 substance Substances 0.000 claims description 11
- 230000002265 prevention Effects 0.000 claims description 5
- 239000000463 material Substances 0.000 abstract description 12
- 229920000642 polymer Polymers 0.000 description 5
- 238000004140 cleaning Methods 0.000 description 4
- 238000002156 mixing Methods 0.000 description 4
- 239000000571 coke Substances 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 238000006068 polycondensation reaction Methods 0.000 description 2
- 238000006116 polymerization reaction Methods 0.000 description 2
- 239000002002 slurry Substances 0.000 description 2
- 239000004952 Polyamide Substances 0.000 description 1
- 238000013019 agitation Methods 0.000 description 1
- 150000001336 alkenes Chemical class 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- -1 diene hydrocarbons Chemical class 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000000295 fuel oil Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 230000002452 interceptive effect Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000000178 monomer Substances 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 229920002647 polyamide Polymers 0.000 description 1
- 229920000728 polyester Polymers 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 238000005979 thermal decomposition reaction Methods 0.000 description 1
- 238000004804 winding Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/0006—Controlling or regulating processes
- B01J19/002—Avoiding undesirable reactions or side-effects, e.g. avoiding explosions, or improving the yield by suppressing side-reactions
- B01J19/0026—Avoiding carbon deposits
-
- 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
- B29B7/46—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with more than one shaft
- B29B7/48—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with more than one shaft with intermeshing devices, e.g. screws
- B29B7/481—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with more than one shaft with intermeshing devices, e.g. screws provided with paddles, gears or discs
-
- 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
- B29B7/80—Component parts, details or accessories; Auxiliary operations
- B29B7/82—Heating or cooling
- B29B7/826—Apparatus therefor
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
- Polymerisation Methods In General (AREA)
- Other Resins Obtained By Reactions Not Involving Carbon-To-Carbon Unsaturated Bonds (AREA)
Abstract
Description
【発明の詳細な説明】
[産業上の利用分野〕
本発明は高粘度流体、スラリー状物質、 tlA体など
の各種状態の物質を撹拌混和するための反応装置に係り
、特に、オレフィン系、共役ジエン系炭化水素などの重
合性有機化合物を付加重金により重合体を得たり、ポリ
アミド、ポリエステルなどの重縮合系重合体を製造する
ための重合反応装置及び重合体から溶剤、単量体を取り
除く々めの装置等の重合体製造に適したものに関する。Detailed Description of the Invention [Field of Industrial Application] The present invention relates to a reaction device for stirring and mixing substances in various states such as high viscosity fluids, slurry substances, and tlA bodies, and particularly relates to olefin-based and conjugated substances. Polymerization reaction equipment for obtaining polymers from polymerizable organic compounds such as diene hydrocarbons by addition of heavy metals, and for producing polycondensation polymers such as polyamides and polyesters, and for removing solvents and monomers from polymers. This invention relates to equipment suitable for polymer production, such as equipment for polymer production.
[背景の技術]
一般に、重合反応装置な、どの高粘度流体、スラリー状
物質、粉体等の各種被処理物質の反応装置は、充分な混
合作用と共に、大きな伝熱、速度が要求され、ざらに反
応機能等に支障を来たすtffi物の付着を防止する機
能を有したものが要ψされる。[Background technology] In general, polymerization reactors and other reactors for processing various materials such as high viscosity fluids, slurry materials, powders, etc. require sufficient mixing action, high heat transfer and speed, and require rough mixing. It is necessary to have a function of preventing the adhesion of tffi substances that interfere with the reaction function, etc.
このような付着物としては、例、えば重質油類をルロ熱
・分解すると、熱分解現、象が生じて、ガラス。For example, when heavy oils are heated and decomposed, a thermal decomposition phenomenon occurs, resulting in the formation of glass.
軽質油等の重質分とピッチ、コーク等の重質分が生成さ
れ、そのうち特に重質分を生成する重縮合過程において
、ピッチ、コークが反応壁、加熱管壁等に析出したコー
キングと称するものが問題となる。そのため、従来より
、上記各種の要請を満足させる手段として複数のスクリ
ュー状に撹拌板を組合わせてセルフクリーニング作用を
生起させる型式などが提案されている。Heavy components such as light oil and heavy components such as pitch and coke are produced, and during the polycondensation process that produces particularly heavy components, pitch and coke are deposited on reaction walls, heating tube walls, etc. This is called coking. Things become a problem. Therefore, as a means to satisfy the above-mentioned various demands, methods have been proposed in which a plurality of screw-shaped stirring plates are combined to produce a self-cleaning action.
ところが、従来のこの種の装置では、いずれのものも反
応容器内のセルフクリーニングを対象とする構成のもの
であって、容器の被処理物質出口及びその近傍のセルフ
クリーニングを行なうことが不□可能なために、出口及
びその近傍にコーキングが発生して配管及び制御弁等が
閉塞するという問題:を有していた。However, all conventional devices of this type are configured to self-clean the inside of the reaction vessel, and it is impossible to self-clean the outlet of the substance to be treated in the vessel and its vicinity. As a result, there has been a problem in that coking occurs at the outlet and its vicinity, clogging piping, control valves, etc.
[発明が解決しようとする問題点1
本弁→は、上記の点に鑑みてなされたもので、容器ア出
口及びその近傍におけるコーキングの防止を図り、確実
なセルフクリーニングを実現し得るようにした反応装置
を提供することを目的とする。[Problem to be solved by the invention 1 This valve → was made in view of the above points, and is designed to prevent caulking at the container outlet and its vicinity, thereby realizing reliable self-cleaning. The purpose is to provide a reactor.
[問題点を解決するための手段]
本発明は容器の入口及び出口の中間部に撹拌板に対応し
て所定の間隔に突設された仕切板と、この仕切板にそれ
ぞれ実装される温度検出手段と、この温度検出手段に応
動して被処理物質の前記出口における温度をコーキング
発生防止温度域に制御する温度制御手段とを備えたこと
を特徴とする。[Means for Solving the Problems] The present invention provides partition plates protruding from the middle of the inlet and outlet of the container at predetermined intervals corresponding to the stirring plates, and temperature detection devices mounted on each of the partition plates. and a temperature control means for controlling the temperature of the material to be treated at the outlet to a coking prevention temperature range in response to the temperature detection means.
[作 用]
すなわち、本発明は仕切板を介して処理物質の容器の各
点における温度を検出し、その検出温度に応じて容器の
出口及びその近傍の被処理物質の温度をコーキング発生
防止温度域に制御することにより、出口配管及び制御弁
等の閉1の要因となるコーキングの発生を防止するよう
にしたものである。[Function] That is, the present invention detects the temperature at each point in the container of the material to be treated through the partition plate, and depending on the detected temperature, adjusts the temperature of the material to be treated at the outlet of the container and its vicinity to the coking prevention temperature. This prevents the occurrence of coking, which can cause the outlet piping, control valves, etc. to close.
[実施例]
以下、本発明の実施例についての、図面を参照して詳細
に説明する。[Example] Hereinafter, examples of the present invention will be described in detail with reference to the drawings.
第1図は本発明の一実施例に係る反応装置を示すもので
、入口11及び出口12を両端部に有してた筒体状容器
10には撹拌体を構成する例えば2本の回転軸13及び
14が軸受15,16及び17、′18を介して軸支さ
れて挿着される。この回転軸13及び14は図示しない
回転駆動部により、それぞれ同一方向に同一回転角速度
で回転駆動され、□その容器10内部において複数個ず
つ肉厚内:板形の撹拌板19及び20がそれぞれ串差し
状に取着される。この撹拌板19及び20は例えばその
回転軸13及び14の中心間距離に等しい直径を有する
円であり、それぞれの中心を回転芯として同一方向、同
一回転角速度で回転する場合、相互に自転l動を妨げる
ことが6いようにして送り機能反び撹拌機能を有するよ
ろに配列される。FIG. 1 shows a reaction apparatus according to an embodiment of the present invention, in which a cylindrical container 10 having an inlet 11 and an outlet 12 at both ends has, for example, two rotating shafts constituting a stirring body. 13 and 14 are inserted and supported by bearings 15, 16, 17, and '18. The rotating shafts 13 and 14 are each driven to rotate in the same direction at the same rotational angular velocity by a rotation drive unit (not shown). It is attached in the form of a plug. The stirring plates 19 and 20 are, for example, circles having a diameter equal to the distance between the centers of their rotating shafts 13 and 14, and when rotating in the same direction and at the same rotational angular velocity with their respective centers as rotation cores, they rotate relative to each other. It is arranged in a 6-way structure that has a feeding function and a stirring function so that it is not obstructed.
すなわモ、り窃撹拌板19及び企Oはそのうち人口11
近傍め所定の数が上記回転軸13および14め向転辷連
動して被処理物置を出口方向に移送せしめる被処理物質
送り作用が生起されるように例えば螺旋階段状に配列さ
れ、その他の撹拌板19及び20が撹拌機能のみを有す
るように配列されている。なお、上記容器10はその内
壁断面形状がそれぞれ対応される撹拌板1つ及び20の
最外端回転軌跡またはそれに近い形状に形成されており
、撹拌板19および20の回転運動に連動してセルフク
リーニングされる。Sunawamo, theft agitation board 19 and company O have a population of 11.
A predetermined number of adjacent ones are arranged in a spiral staircase shape, for example, so that a feeding action of the material to be processed is caused by moving the rotating shafts 13 and 14 in the direction of the rotating shafts 13 and 14 to move the material to be processed toward the exit. The plates 19 and 20 are arranged so as to have only a stirring function. The cross-sectional shape of the inner wall of the container 10 is formed in the shape of or close to the outermost rotation locus of the corresponding stirring plate 19 and 20, and the self-winding movement is linked to the rotational movement of the stirring plates 19 and 20. Cleaned.
また、上記容器10には複数の仕切板21乃至28が上
記撹拌板19及び、・20間に所定の間隔を有し・て位
置するように突設される。この仕切板21乃至28はそ
れぞれ撹拌板・19及び20の自転運動を妨げることな
く、軽く接触するかあるいは所定の間隙を有して配設さ
れ、そのうち仕切板21゜24.26.28にはそれ、
ぞれ上記容器10の一端に取着された第1の温度惟出部
29に対応される第2乃至第5の温度検出部30乃至3
3が実装されている。そして、この第1乃至第5の温度
検出部29乃至33の各出力端は第1乃至第5の温度制
御部34乃至38に接、続され、このMl乃至第5の温
度制御Nl34乃至38は第1乃至第5の駆動部39乃
至43を介して上記第1乃至第5の温度検出部29乃至
33に対応して上記容器10にそれぞれ配設されて温度
制御用の第1乃至第5のヒータ44乃至48に接続され
る。なお、上記仕切#i21乃至28はそれぞれ撹拌板
19及び20の回転運動に連動して、該撹拌板19及び
20によりセルフクリーニングされる。Further, a plurality of partition plates 21 to 28 are protruded from the container 10 so as to be spaced apart from each other by a predetermined distance between the stirring plates 19 and 20. The partition plates 21 to 28 are arranged so as to lightly contact or have a predetermined gap between the stirring plates 19 and 20 without interfering with their rotational movement, and among them, the partition plates 21, 24, 26, and 28 are that,
Second to fifth temperature detection units 30 to 3 respectively correspond to the first temperature extraction unit 29 attached to one end of the container 10.
3 has been implemented. The output terminals of the first to fifth temperature detection sections 29 to 33 are connected to the first to fifth temperature control sections 34 to 38, and the M1 to fifth temperature control sections N1 to 38 are The first to fifth temperature detecting units 29 to 43 are arranged in the container 10 to correspond to the first to fifth temperature detecting units 29 to 33 via the first to fifth driving units 39 to 43, respectively, for temperature control. It is connected to heaters 44 to 48. Note that the partitions #i21 to #i28 are self-cleaned by the stirring plates 19 and 20 in conjunction with the rotational movement of the stirring plates 19 and 20, respectively.
すなわち、上記反応装置は上記回転駆動部(図示せず)
が駆動されて回転軸13及び14が回転駆動されると、
その撹拌板19及び20の作用により、容器10内の被
処理物質を仕切板21乃至2日を乗り越えさせて出口方
向に移送しながら攪拌して混合あるいは反応を行ないせ
しめる。このとき、第1乃至第5の温度検出部29乃至
33はそれぞれ容器10の一端の温度、仕切板21゜2
4.26.2’8の位置における被処理物質の温度を検
出して各検出信号をそれぞれ第1乃至第5の温度制御部
34乃至38に出力する。すると、この第1乃至第5の
温度制御部34乃至38はそれぞれ第1乃至第5の駆動
部39乃至43を介して第1乃至第5のヒータ44乃至
48を駆動制御し、第1乃至第4の温度検出部29乃至
32における温度を混合あるいは反応に適した温度(例
えば450℃程度)に制砥するとともに、第5の温度検
出部33における温度をコーキング発生防止温度域(例
えば350℃程度)に制御せしめる。That is, the reaction device includes the rotational drive section (not shown).
is driven and the rotating shafts 13 and 14 are rotationally driven,
Due to the action of the stirring plates 19 and 20, the substance to be treated in the container 10 is moved over the partition plates 21 to 22 and transferred toward the outlet while being stirred and mixed or reacted. At this time, the first to fifth temperature detection units 29 to 33 detect the temperature at one end of the container 10, respectively, and the partition plate 21°2.
4.26. The temperature of the substance to be processed at the position 2'8 is detected and each detection signal is output to the first to fifth temperature control sections 34 to 38, respectively. Then, the first to fifth temperature control sections 34 to 38 drive and control the first to fifth heaters 44 to 48 via the first to fifth drive sections 39 to 43, respectively. The temperature in the fourth temperature detection part 29 to 32 is controlled to a temperature suitable for mixing or reaction (for example, about 450°C), and the temperature in the fifth temperature detection part 33 is controlled to a coking prevention temperature range (for example, about 350°C). ).
これにより、上記容器10は出口12及びその近傍にお
いても、被処理物質がコーキング発生防止温度域に制御
されていることで、撹拌板1つ及び20のセルフクリー
ニング作用による内壁部と同様にコーキングの発生が防
止される。As a result, since the substance to be treated is controlled to a temperature range that prevents coking at the outlet 12 and its vicinity, coking is prevented in the container 10 as well as on the inner wall due to the self-cleaning action of one stirring plate and 20. Occurrence is prevented.
なお、この発明は上記実施例に限定されるものではなく
、その他、この発明の要旨を逸脱しない範囲で種々の変
形を実施し得ることはいうまでもないことである。It goes without saying that the present invention is not limited to the above-mentioned embodiments, and that various modifications can be made without departing from the gist of the present invention.
[発明の効果コ
以上詳述したように、本発明によれば仕切板を介して処
理物質の容器の各点における温度を検出し、その検出温
度に応じて容器の出口及びその近傍の処理物質のm度を
コーキング発生防止温度域に制御するように構成したの
で、容器の出口及びその近傍におけるコーキングの防止
が図れて確実なセルフクリーニングが実現された反応装
置を提供することができる。[Effects of the Invention] As described in detail above, according to the present invention, the temperature at each point in the container for the material to be treated is detected through the partition plate, and the temperature at the outlet of the container and the vicinity thereof is adjusted according to the detected temperature. Since the temperature is controlled to be within the coking prevention temperature range, it is possible to provide a reaction apparatus that prevents coking at the outlet of the container and its vicinity and achieves reliable self-cleaning.
第1図はこの発明の一実施例に係る反応装置を示す構成
説明図である。
10・・・容器、11・・・入口、12・・・出口、1
3゜14・・・回転軸、15,16,17.18・・・
軸受、19.20・・・撹拌板、21乃至28・・・仕
切板、2つ乃至33・・・第1乃至第5の温度検出部、
34乃至38・・・第1乃至第5の温度制御部、39乃
至43・・・第1乃至第5の駆動部、44乃至48・・
・第1乃至第5のヒータ。FIG. 1 is a structural explanatory diagram showing a reaction apparatus according to an embodiment of the present invention. 10... Container, 11... Inlet, 12... Outlet, 1
3゜14...rotation axis, 15, 16, 17.18...
Bearing, 19.20... Stirring plate, 21 to 28... Partition plate, 2 to 33... First to fifth temperature detection parts,
34 to 38...first to fifth temperature control units, 39 to 43...first to fifth drive units, 44 to 48...
-First to fifth heaters.
Claims (1)
れぞれ板面を垂直に串差し状に連結した複数の撹拌板で
構成された撹拌体と、前記回転軸と撹拌体を収納してな
るもので、被処理物質の入口及び出口を有し、かつ撹拌
体の最外端軌跡に等しいか又は僅かに大きい内腔を有す
る容器とからなり前記被処理物質を循環させながら混合
あるいは反応させてなる反応装置において、前記容器の
入口及び出口の中間部に前記撹拌板に対応して所定の間
隔に突設された仕切板と、この仕切板にそれぞれ実装さ
れる温度検出手段と、この温度検出手段に応動して前記
被処理物質の前記出口における温度をコーキング発生防
止温度域に制御する温度制御手段とを具備したことを特
徴とする反応装置。A stirring body composed of a plurality of rotating shafts arranged parallel to each other, a plurality of stirring plates each having a plate surface perpendicularly connected to each rotating shaft in a skewer shape, and housing the rotating shafts and the stirring body. It consists of a container having an inlet and an outlet for the substance to be treated, and a lumen that is equal to or slightly larger than the outermost locus of the stirring body, and the substance to be treated is mixed or reacted while being circulated. A reaction apparatus comprising: a partition plate protruding at a predetermined interval between an inlet and an outlet of the container corresponding to the stirring plate; a temperature detection means mounted on each of the partition plates; A reaction apparatus comprising: a temperature control means for controlling the temperature at the outlet of the substance to be treated to a coking prevention temperature range in response to the detection means.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61019573A JPS62180746A (en) | 1986-01-31 | 1986-01-31 | Reaction device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61019573A JPS62180746A (en) | 1986-01-31 | 1986-01-31 | Reaction device |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS62180746A true JPS62180746A (en) | 1987-08-08 |
Family
ID=12003024
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP61019573A Pending JPS62180746A (en) | 1986-01-31 | 1986-01-31 | Reaction device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS62180746A (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0858829A2 (en) * | 1997-01-15 | 1998-08-19 | Hoechst Aktiengesellschaft | High surface intermeshing profile reactor |
US5816697A (en) * | 1995-12-05 | 1998-10-06 | Teijin Limited | Viscous liquid stirring device and a process for producing polycarbonate by using the stirring device |
EP0896832A1 (en) * | 1997-08-12 | 1999-02-17 | Hoechst Aktiengesellschaft | High surface intermeshing profile reactor and use thereof |
EP0897742A1 (en) * | 1997-08-12 | 1999-02-24 | Hoechst Research & Technology Deutschland GmbH & Co. KG | High surface intermeshing profile reactor and use thereof |
CN104877129A (en) * | 2015-06-25 | 2015-09-02 | 安庆市虹泰新材料有限责任公司 | Polyamide production system |
-
1986
- 1986-01-31 JP JP61019573A patent/JPS62180746A/en active Pending
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5816697A (en) * | 1995-12-05 | 1998-10-06 | Teijin Limited | Viscous liquid stirring device and a process for producing polycarbonate by using the stirring device |
EP0858829A2 (en) * | 1997-01-15 | 1998-08-19 | Hoechst Aktiengesellschaft | High surface intermeshing profile reactor |
EP0858829A3 (en) * | 1997-01-15 | 1999-03-17 | Hoechst Aktiengesellschaft | High surface intermeshing profile reactor |
EP0896832A1 (en) * | 1997-08-12 | 1999-02-17 | Hoechst Aktiengesellschaft | High surface intermeshing profile reactor and use thereof |
EP0897742A1 (en) * | 1997-08-12 | 1999-02-24 | Hoechst Research & Technology Deutschland GmbH & Co. KG | High surface intermeshing profile reactor and use thereof |
CN104877129A (en) * | 2015-06-25 | 2015-09-02 | 安庆市虹泰新材料有限责任公司 | Polyamide production system |
CN104877129B (en) * | 2015-06-25 | 2017-03-15 | 安庆市虹泰新材料有限责任公司 | A kind of polyamide production system |
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