DE202006003429U1 - Depolymerization device for polymerizing raw materials containing hydrocarbons, such as residues, comprises agitator, a reactor, mixing element of the self-cleaning element intended for cyclic removal of deposits from the reactor - Google Patents
Depolymerization device for polymerizing raw materials containing hydrocarbons, such as residues, comprises agitator, a reactor, mixing element of the self-cleaning element intended for cyclic removal of deposits from the reactor Download PDFInfo
- Publication number
- DE202006003429U1 DE202006003429U1 DE200620003429 DE202006003429U DE202006003429U1 DE 202006003429 U1 DE202006003429 U1 DE 202006003429U1 DE 200620003429 DE200620003429 DE 200620003429 DE 202006003429 U DE202006003429 U DE 202006003429U DE 202006003429 U1 DE202006003429 U1 DE 202006003429U1
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- Germany
- Prior art keywords
- scraping
- reactor
- self
- cleaning
- mixer
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- Expired - Lifetime
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J11/00—Recovery or working-up of waste materials
- C08J11/04—Recovery or working-up of waste materials of polymers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/04—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping pipe stills
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/14—Fractional distillation or use of a fractionation or rectification column
- B01D3/32—Other features of fractionating columns ; Constructional details of fractionating columns not provided for in groups B01D3/16 - B01D3/30
- B01D3/322—Reboiler specifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/05—Stirrers
- B01F27/051—Stirrers characterised by their elements, materials or mechanical properties
- B01F27/053—Stirrers characterised by their elements, materials or mechanical properties characterised by their materials
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/05—Stirrers
- B01F27/09—Stirrers characterised by the mounting of the stirrers with respect to the receptacle
- B01F27/091—Stirrers characterised by the mounting of the stirrers with respect to the receptacle with elements co-operating with receptacle wall or bottom, e.g. for scraping the receptacle wall
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/05—Stirrers
- B01F27/11—Stirrers characterised by the configuration of the stirrers
- B01F27/112—Stirrers characterised by the configuration of the stirrers with arms, paddles, vanes or blades
- B01F27/1122—Stirrers characterised by the configuration of the stirrers with arms, paddles, vanes or blades anchor-shaped
-
- 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
- B01J19/0053—Details of the reactor
- B01J19/0066—Stirrers
-
- 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
- B01J19/18—Stationary reactors having moving elements inside
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G1/00—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
- C10G1/10—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal from rubber or rubber waste
-
- 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
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00051—Controlling the temperature
- B01J2219/00074—Controlling the temperature by indirect heating or cooling employing heat exchange fluids
- B01J2219/00087—Controlling the temperature by indirect heating or cooling employing heat exchange fluids with heat exchange elements outside the reactor
- B01J2219/00094—Jackets
-
- 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
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00051—Controlling the temperature
- B01J2219/00157—Controlling the temperature by means of a burner
-
- 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
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00761—Details of the reactor
- B01J2219/00763—Baffles
- B01J2219/00779—Baffles attached to the stirring means
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/141—Feedstock
- Y02P20/143—Feedstock the feedstock being recycled material, e.g. plastics
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/62—Plastics recycling; Rubber recycling
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Wood Science & Technology (AREA)
- General Chemical & Material Sciences (AREA)
- Sustainable Development (AREA)
- Health & Medical Sciences (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Accessories For Mixers (AREA)
- Mixers Of The Rotary Stirring Type (AREA)
Abstract
Description
Die Erfindung betrifft eine Depolymerisationsanlage für kohlenwasserstoffhaltige Rohmaterialien mit einem einen Rührer aufweisenden, außen beheizten Reaktor.The The invention relates to a depolymerization plant for hydrocarbon-containing Raw materials with a stirrer having, outside heated Reactor.
Bei der Depolymerisation von kohlenwasserstoffhaltigen Rückständen, insbesondere zur Erzeugung von Dieselöl, werden die Rohmaterialien, wie Alt-, Abfall- oder Rückstandsmaterialien mit oder ohne Katalysatoranwendung bei Temperaturen zwischen 300 und 450°C depolymerisiert, d.h., die Molekühle langkettiger Kohlenwasserstoffverbindungen werden gespalten. Die Spaltprodukte verdampfen und werden zu dem Endprodukt weiterbehandelt, z.B. destilliert. Flüssig oder fest verbleibende, so genannte Sumpfprodukte, werden aus dem Reaktor ausgeschleust. Die Reaktorinnentemperatur wird mit Hilfe eines Rührers vergleichmäßigt. Zusätzlich oder alternativ zum Rühren kann die Reaktorwand durch Schabeelement zyklisch von Ablagerungen befreit werden. Die Einhaltung einer bestimmten Reaktorinnentemperatur ist für die Kontinuität des Depolymerisationsprozesses von großer Bedeutung. Lokale Temperaturüberschreitungen, aber auch Änderungen in der Rohmaterialzusammensetzung führen in der Regel zu Ablagerungen oder Anbackungen, insbesondere von Kohlenstoff an den Reaktorin nenwänden und an den Mischerelementen bzw. den Schabeelementen, so dass Prozessstörungen und -unterbrechungen auftreten und der Reaktor bzw. die Rühr- oder Schabeelemente gereinigt oder ausgetauscht werden müssen.at the depolymerization of hydrocarbon-containing residues, in particular for the production of diesel oil, become the raw materials, such as waste, waste or residue materials with or without catalyst application at temperatures between 300 and 450 ° C depolymerizes, i.e., the molecules long-chain hydrocarbon compounds are split. The Fission products evaporate and are further treated to the final product, e.g. distilled. Liquid or remaining, so-called bottoms, are extracted from the Discharged reactor. The internal reactor temperature is using a stirrer uniform. Additionally or alternatively to stir The reactor wall can cyclically by scraping element of deposits be freed. The maintenance of a certain internal reactor temperature is for the continuity the depolymerization process of great importance. Local temperature overruns, but also changes in the raw material composition usually lead to deposits or caking, in particular of carbon on the reactor walls and nenin at the mixer elements or the scraping elements, so that process disturbances and interruptions occur and the reactor or the stirring or scraping cleaned or need to be replaced.
Um
die Verfügbarkeit
gattungsgemäßer Depolymerisationsanlagen
zu verbessern, wird. erfindungsgemäß eine Depolymerisationsanlage
mit den Merkmalen des Anspruchs 1 vorgeschlagen. Demgemäß ist ein
Selbstreinigungselement vorgesehen, dass der Reaktor (
Die Selbstreinigung erfolgt besonders wirkungsvoll unter gegenseitiger Anlage des Selbstreinigungselementes an dem Mischerelement oder dem Schabeelement. Eine derartige Relativbewegung kann quer zu einer zu reinigenden Kante erfolgen. Es kann aber auch ein Selbstreinigungskopf entlang der zu reinigenden Kante oder Fläche verfahren werden.The Self-cleaning is particularly effective with mutual Plant of the self-cleaning element on the mixer element or the cockroach element. Such relative movement can transverse to a to be cleaned edge. But it can also be a self-cleaning head be moved along the edge or surface to be cleaned.
Die Betätigung des Selbstreinigungselementes ist besonders einfach, wenn ein Antriebselement entlang eines Rotationsschaftes des Schabers oder Rührers verschiebbar ist, der z. B. eine teleskopartige Bewegung relativ zum Rotationsschaft ausführt.The activity the self-cleaning element is particularly simple when a drive element along a rotational shaft of the scraper or stirrer is displaceable, the z. B. performs a telescopic movement relative to the rotation shaft.
Erfindungsgemäße Selbstreinigungsmittel eigen sich insbesondere für Reaktoren mit einer rotationssymmetrischer und/oder etwa balliger Innenkontur.Own self-cleaning agent according to the invention especially for Reactors with a rotationally symmetric and / or approximately spherical Inner contour.
Die Verwendung temperaturbeständiger Keramik- oder Graphitwerkstoffe für das Mischerelement, das Schabeelement oder das Selbstreinigungselement verbessern die Langzeitverwendbarkeit. The Use temperature resistant Ceramic or graphite materials for the mixer element, the scraper element or the self-cleaning element improves the long-term usability.
Besonders wirkungsvoll sind selbstreinigende Schabeelemente, wenn sie Bestandteil eines Schabekopfes sind, der mit seinem Eigengewicht und/oder mittels einer über den Rotationsschaft aufrecht erhaltenen Druckkraft an die Innenwand des Reaktors anlegbar ist. Rotationsköpfe oder – schäfte, die eine Bewegung des Schabekopfes in axialer Richtung gestatten, wie eine steckbare Drehantriebsverbindung, gestatten es, den Verschleiß der Schabeelemente auszugleichen und somit eine dauerhafte Anlage an der Reaktorinnenwand mit geringem Abstandsspiel zu ermöglichen. Wenn der Schabekopf einer Aufnahme für einen als Verschleißteil ausgebildetes Schalelement aufweist, vereinfacht sich die Materialauswahl für die verschiedenen Bestandteile des Schabekopfes, insbesondere die Optimierung des Verschleißverhaltens der Schabeelemente und der Schonung der Reaktorinnenwand. Der zunehmende Verschleiß der Schabeelemente wird vorzugsweise überwacht, z.B. kann das Erreichen eines Grenzverschleißwertes überwacht werden. Hierzu können insbesondere elektrische Kontakte verwendet werden. Besonders bevorzugt bildet das Schabeelement den einen Kontakt und eine Aufnahme des Schabeelementes den Gegenkontakt. Hierzu sind beide Elemente elektrisch gegeneinander isoliert. Diese beiden Kontakte können z.B. durch die Reaktorwand selbst überbrückt werden, wenn das Schabeelement entsprechend weit verschlissen ist.Especially Self-cleaning scraper elements are effective if they are part of it a scraper head, with its own weight and / or by means of one over the rotation shaft maintained compressive force against the inner wall of the reactor can be applied. Rotary heads or shafts that cause movement of the Allow scraping head in the axial direction, such as a pluggable rotary drive connection, allow the wear of the Balancing scraper elements and thus a permanent investment allow the reactor inner wall with a small clearance clearance. When the scraping head of a receptacle for a trained as wearing part Having shell element, simplifies the choice of materials for the different Components of the scraping head, in particular the optimization of the wear behavior the scraping elements and the conservation of the reactor inner wall. The increasing Wear the Cockroaches are preferably monitored, e.g. can achieve that monitored a limit wear value become. You can do this in particular electrical contacts are used. Especially preferred the scraper element forms a contact and a receptacle of the scraper element the counter contact. For this purpose, both elements are electrically against each other isolated. These two contacts can e.g. through the reactor wall be bridged by yourself, if the cocking element is worn correspondingly far.
Die vorgenannten sowie die beanspruchten und in den Ausführungsbeispielen beschriebenen erfindungsgemäß zu verwendenden Bauteile unterliegen in ihrer Größe, Formgestaltung, Materialauswahl und technischen Konzeption keinen besonderen Ausnahmebedingungen, so dass die in dem Anwendungsgebiet bekannten Auswahlkriterien uneingeschränkt Anwendung finden könnenThe the aforementioned and the claimed and in the embodiments described to be used according to the invention Components are subject in size, shape design, Material selection and technical conception no special exceptions, so that the selection criteria known in the field of application apply without restriction can find
Weitere Einzelheiten, Merkmale und Vorteile des Gegenstandes der Erfindung ergeben sich aus den Unteransprüchen, sowie aus der nachfolgenden Beschreibung der zuge hörigen Zeichnung und Tabelle, in der – beispielhaft – ein Ausführungsbeispiel einer Depolymerisationsanlage dargestellt ist. Further details, features and advantages of the subject matter of the invention will become apparent from the dependent claims, as well as from the following description of the impaired drawing and table in which - by way of example - an embodiment of a Depolymerisationsanlage is shown.
In der Zeichnung zeigen.In show the drawing.
Wie
aus
Bei
dem in
Im Übrigen können die
Schabeelemente in sehr verschiedener Weise ausgebildet sein. Bei
dem Ausführungsbeispiel
nach
- 11
- Rohmaterialraw material
- 22
- Vorwärmstufepreheating
- 2A2A
- Entspannungsstufeexpansion stage
- 33
- Einspritzunginjection
- 44
- Reaktorreactor
- 4A4A
- Gasraumheadspace
- 4B4B
- Sumpfswamp
- 4B'4B '
- Wandungwall
- 4C4C
- Innenwandinner wall
- 4D4D
- Reaktordeckelreactor cover
- 4E4E
- Außenwandouter wall
- 4F4F
- Strömungsleitelementeflow guide
- 4G4G
- Reaktortopfreactor pot
- 4G'4G '
- MündungsflanschMündungsflansch
- 4H4H
- Rohmaterialeinspeisungraw material feed
- 4J4J
- Austragsschleuseairlock
- 55
- Beheizungheating
- 5A5A
- Heizmantelheating jacket
- 5A'5A '
- Flanschflange
- 5B5B
- Zwischenbodenfalse floor
- 5C5C
- Leitungmanagement
- 5D5D
- Mischermixer
- 5E5E
- Gebläsefan
- 5F5F
- Abzugdeduction
- 66
- Produktproduct
- 77
- Reststoffwaste material
- 88th
- Rührerstirrer
- 8A8A
- Armepoor
- 8B8B
- Mischerelementemixer elements
- 99
- Destillationskolonnedistillation column
- 1010
- SchabeeinrichtungScraper means
- 10A10A
- Armepoor
- 10B10B
- Flügelwing
- 10C10C
- Schabeelementescraper
- 10D10D
- SchabekopfSchabekopf
- 10E10E
- Rotationsschaftrotary shaft
- 10F10F
- Aufnahmeadmission
- 10G10G
- SelbstreinigungselementSelf-cleaning element
- 10G'10G '
- Schabekantescraping
- 10G''10G ''
- SelbstreinigungskopfSelf-cleaning head
- 10H10H
- Antriebselementdriving element
- 1212
- VerschleißerfassungseinrichtungWear detector
- 12A12A
- TrennschichtInterface
- AA
- Doppelpfeiledouble arrows
- SS
- Abstandsspaltclearance gap
- MM
- Motorengine
- RR
- Doppelpfeiledouble arrows
Claims (19)
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE200620003429 DE202006003429U1 (en) | 2006-03-02 | 2006-03-02 | Depolymerization device for polymerizing raw materials containing hydrocarbons, such as residues, comprises agitator, a reactor, mixing element of the self-cleaning element intended for cyclic removal of deposits from the reactor |
PCT/EP2007/001771 WO2007098949A1 (en) | 2006-03-02 | 2007-03-01 | Depolymerisation installation and method for the depolymerisation of raw materials containing hydrocarbon |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE200620003429 DE202006003429U1 (en) | 2006-03-02 | 2006-03-02 | Depolymerization device for polymerizing raw materials containing hydrocarbons, such as residues, comprises agitator, a reactor, mixing element of the self-cleaning element intended for cyclic removal of deposits from the reactor |
Publications (1)
Publication Number | Publication Date |
---|---|
DE202006003429U1 true DE202006003429U1 (en) | 2007-07-05 |
Family
ID=38282571
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
DE200620003429 Expired - Lifetime DE202006003429U1 (en) | 2006-03-02 | 2006-03-02 | Depolymerization device for polymerizing raw materials containing hydrocarbons, such as residues, comprises agitator, a reactor, mixing element of the self-cleaning element intended for cyclic removal of deposits from the reactor |
Country Status (1)
Country | Link |
---|---|
DE (1) | DE202006003429U1 (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2010106009A1 (en) | 2009-03-16 | 2010-09-23 | Vit Environmentsystems Ag | Device for thermal treatment, in particular thermal decomposition of waste oil mixtures |
DE102012204648A1 (en) | 2012-03-22 | 2013-09-26 | Wilfried Schraufstetter | Device useful for liquefying hydrocarbon-containing waste materials, comprises cylindrical reactor chamber with first lid, second lid and cladding, feed screw and agitator comprising agitator shaft along cylindrical axis of reactor chamber |
CN108816168A (en) * | 2018-04-26 | 2018-11-16 | 南通三圣石墨设备科技股份有限公司 | A kind of integral type graphiote reactor |
CN113058533A (en) * | 2021-04-21 | 2021-07-02 | 江西和正建材有限公司 | Preparation process of negative oxygen ion coating |
-
2006
- 2006-03-02 DE DE200620003429 patent/DE202006003429U1/en not_active Expired - Lifetime
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2010106009A1 (en) | 2009-03-16 | 2010-09-23 | Vit Environmentsystems Ag | Device for thermal treatment, in particular thermal decomposition of waste oil mixtures |
DE102012204648A1 (en) | 2012-03-22 | 2013-09-26 | Wilfried Schraufstetter | Device useful for liquefying hydrocarbon-containing waste materials, comprises cylindrical reactor chamber with first lid, second lid and cladding, feed screw and agitator comprising agitator shaft along cylindrical axis of reactor chamber |
CN108816168A (en) * | 2018-04-26 | 2018-11-16 | 南通三圣石墨设备科技股份有限公司 | A kind of integral type graphiote reactor |
CN113058533A (en) * | 2021-04-21 | 2021-07-02 | 江西和正建材有限公司 | Preparation process of negative oxygen ion coating |
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Legal Events
Date | Code | Title | Description |
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R207 | Utility model specification |
Effective date: 20070809 |
|
R150 | Utility model maintained after payment of first maintenance fee after three years |
Effective date: 20090616 |
|
R157 | Lapse of ip right after 6 years |
Effective date: 20121002 |