EP0337579B1 - Brikettbindemittel - Google Patents
Brikettbindemittel Download PDFInfo
- Publication number
- EP0337579B1 EP0337579B1 EP89200939A EP89200939A EP0337579B1 EP 0337579 B1 EP0337579 B1 EP 0337579B1 EP 89200939 A EP89200939 A EP 89200939A EP 89200939 A EP89200939 A EP 89200939A EP 0337579 B1 EP0337579 B1 EP 0337579B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- binder
- component
- weight
- briquettes
- binder according
- 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.)
- Expired - Lifetime
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
- C10L5/00—Solid fuels
- C10L5/02—Solid fuels such as briquettes consisting mainly of carbonaceous materials of mineral or non-mineral origin
- C10L5/06—Methods of shaping, e.g. pelletizing or briquetting
- C10L5/10—Methods of shaping, e.g. pelletizing or briquetting with the aid of binders, e.g. pretreated binders
- C10L5/14—Methods of shaping, e.g. pelletizing or briquetting with the aid of binders, e.g. pretreated binders with organic binders
- C10L5/16—Methods of shaping, e.g. pelletizing or briquetting with the aid of binders, e.g. pretreated binders with organic binders with bituminous binders, e.g. tar, pitch
Definitions
- the present invention relates to a binder which is suitable for the production of briquettes, to the use of this binder for the production of briquettes and to briquettes that are produced by using this binder.
- a coal briquette on the one hand, should be able to gently glow under conditions where relatively little combustibles and oxygen are present, whereas under other conditions the briquette should be able to burn with a clear flame and not fall apart unburned. This may be expressed as fuel efficiency in terms of the coal content of the ashes.
- Another aspect of the burning behaviour is that a good fuel efficiency is required.
- the former aspect of the burning behaviour can also be viewed as a mechanical requirement for the binder, i.e. the binder should be able to confer to the briquette during burning enough strength that it will not fall apart until used up for the greater part.
- the (national) criteria regarding the the emission of environmentally objectionable substances should be met.
- the selection of the binder is also determined by the sulfur content, the ash content and the emission of compounds during combustion or other processing.
- Smell is a criterion which is more subjective than the above-mentioned criteria. It has been found, for example, that the acceptance of coal briquettes for domestic use largely depends on the extent to which the binder and the briquette give off an undesirable smell under storage or usage conditions. Strongly smelling briquettes generally are not accepted. This is, of course, related to the fact that the briquettes are often stored in storage spaces which often are badly ventilated, such as in basements, and in the proximity of food such as potatoes or other personal effects.
- GB-A-960 921 does not disclose the use of components obtained from the steam cracking of light hydrocarbons.
- the binder which is suitable for the production of briquettes or shaped forms, comprises
- One preferred way to modify the polyaromatic pyrolysis oil is to substantially remove the low molecular fraction from the oil to obtain a pyrolysis oil fraction with a more narrow molecular weight distribution which improves the adhesive strenght and affinity with respect to the fines that are to be briquetted.
- this concerns reducing the fraction having a molecular weight (determined by GPC in THF) smaller than 1000, so that a product remains having a ring and ball softening point of at least 100°C, preferably 110-170°C.
- the binder is preferably substantially free of ashes, minerals, metals and in particular free of elements of the group IIIA and VA of the Periodic System of Elements, or compounds thereof.
- substantially free is meant that the content of the respective component is not higher than 0.05% by weight, based on the binder.
- the binder according to the invention has an excellent homogeneity and stability. More particularly, the binder fulfils the requirements of Dutch standard NEN 3965, which means, among other things, that no phase separation takes place during storage.
- This product was mixed at 175°C with 15% by weight (based on the total binder) of a mixture (1/1) of vacuum residue and vacuum distillate.
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Geochemistry & Mineralogy (AREA)
- Geology (AREA)
- Environmental & Geological Engineering (AREA)
- Life Sciences & Earth Sciences (AREA)
- Organic Chemistry (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Solid Fuels And Fuel-Associated Substances (AREA)
- Transition And Organic Metals Composition Catalysts For Addition Polymerization (AREA)
- Working-Up Tar And Pitch (AREA)
- Dental Preparations (AREA)
- Medicines Containing Antibodies Or Antigens For Use As Internal Diagnostic Agents (AREA)
- Non-Silver Salt Photosensitive Materials And Non-Silver Salt Photography (AREA)
- Manufacture And Refinement Of Metals (AREA)
Claims (13)
- Bindemittel zur Verwendung bei der Herstellung von Briketts oder Formkörpern, umfassenda) eine, gegebenenfalls modifizierte, polyaromatische Komponente, die als Primärkondensat beim Dampfcracken von leichten Kohlenwasserstoffen erhalten wird,b) mindestens eine Komponente, ausgewählt aus der Gruppe, bestehend aus atmosphärischen und Vakuumrückständen und Destillaten, die beim Raffinieren und/oder (Hydro)Cracken von Erdöl oder Erdölfraktionen erhalten werden.
- Bindemittel nach Anspruch 1, umfassend 75 bis 95 Gew.-Teile von Komponente a) und 25 bis 5 Gew.-Teile von Komponente b).
- Bindemittel nach Anspruch 1 oder 2, worin Komponente a) beim Dampfcracken von LPG, Gasöl oder Naphtha erhalten wird.
- Bindemittel nach einem der Ansprüche 1 bis 3, worin Komponente a) das durch das katalytische oder thermische Dampfcracken von leichten Kohlenwasserstoffen bei einer Temperatur von 700 bis 2000°C erhaltene Produkt ist, aus dem die Komponenten, die bei atmosphärischem Druck gasförmig sind, entfernt werden.
- Bindemittel nach einem der Ansprüche 1 bis 4, worin Komponente a) einer Extraktion, Destillation, Flokkulation/Präzipitation oder oxidativen Behandlung oder einer Kombination von zwei oder mehreren davon unterzogen worden ist.
- Bindemittel nach einem der Ansprüche 1 bis 5, worin Komponente b) 40 bis 100 Gew.-% eines Vakuumrückstands aus dem Erdölraffinieren und 60 bis 0 Gew.-% eines Vakuumdestillats aus dem Erdölraffinieren enthält.
- Bindemittel nach einem der Ansprüche 1 bis 6, weiterhin umfassend 60 Gew.-% Mineralöl oder schweres Gasöl, bezogen auf Komponente b).
- Bindemittel nach einem der Ansprüche 1 bis 7, weiterhin umfassend 0,2 bis 10 Gew.-% ataktisches Polypropylen- oder Polyethylenwachs oder eine Kombination davon, bezogen auf das Gewicht des Bindemittels.
- Verwendung des Bindemittels nach einem der Ansprüche 1 bis 8 zur Herstellung von Briketts.
- Brikett, umfassend ein Bindemittel nach einem der Ansprüche 1 bis 8 und eine gebundene Substanz.
- Brikett nach Anspruch 10, worin der Bindemittelgehalt zwischen 1 und 20 Gew.-%, bezogen auf das Brikett, liegt.
- Brikett nach Anspruch 10 oder 11, worin die gebundene Substanz aus der Gruppe, bestehend aus Kohle, Magnesiumoxid, Magnesiumcarbonat, Koks, mit Metall angereichertem Staub, Quarzsand und Mischungen von zwei oder mehreren dieser Produkte ausgewählt ist.
- Verfahren zur Herstellung des Bindemittels nach einem der Ansprüche 1 bis 8, worin die Komponenten a) und b) bei einer Temperatur oberhalb des Erweichungspunktes des Bindemittels vermischt werden.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| AT89200939T ATE82019T1 (de) | 1988-04-15 | 1989-04-14 | Brikettbindemittel. |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| NL8800980 | 1988-04-15 | ||
| NL8800980 | 1988-04-15 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| EP0337579A1 EP0337579A1 (de) | 1989-10-18 |
| EP0337579B1 true EP0337579B1 (de) | 1992-11-04 |
Family
ID=19852135
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| EP89200939A Expired - Lifetime EP0337579B1 (de) | 1988-04-15 | 1989-04-14 | Brikettbindemittel |
Country Status (4)
| Country | Link |
|---|---|
| EP (1) | EP0337579B1 (de) |
| AT (1) | ATE82019T1 (de) |
| DE (1) | DE68903352T2 (de) |
| ES (1) | ES2036022T3 (de) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106701236B (zh) * | 2017-01-24 | 2019-05-31 | 福州大学 | 利用垃圾渗滤液制备型煤粘结剂及其生产工业型煤的方法 |
Family Cites Families (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE890183C (de) * | 1941-02-07 | 1953-09-17 | Gelsenkirchener Bergwerks Ag | Verwendung von aus Pechen gewonnenen Massen zur Brikettierung |
| GB759145A (en) * | 1952-03-29 | 1956-10-17 | Gelsenkirchener Bergwerks Ag | Improvements in or relating to briquetting |
| FR1274660A (fr) * | 1960-09-16 | 1961-10-27 | Raffinage Cie Francaise | Procédé de préparation de bitumes de pétrole, convenant à la fabrication de combustibles agglomérés, et produits en résultant |
| DE1645735A1 (de) * | 1967-10-07 | 1970-12-23 | Esso Res And Engineering Co | Verfahren zur Herstellung von Kohlebindemitteln |
| DE2708495C2 (de) * | 1977-02-26 | 1982-10-14 | Rütgerswerke AG, 6000 Frankfurt | Verwendung von Pech als Bindemittel für Steinkohlenbriketts |
-
1989
- 1989-04-14 ES ES198989200939T patent/ES2036022T3/es not_active Expired - Lifetime
- 1989-04-14 DE DE8989200939T patent/DE68903352T2/de not_active Expired - Fee Related
- 1989-04-14 EP EP89200939A patent/EP0337579B1/de not_active Expired - Lifetime
- 1989-04-14 AT AT89200939T patent/ATE82019T1/de not_active IP Right Cessation
Non-Patent Citations (5)
| Title |
|---|
| Erdöl und Kole - Erdgas - Petrochemie vereinigt mit Brennstoff-chemie, Bd. 38, Heft 1, January 1985. * |
| Erdöl und Kole - Erdgas - Petrochemie vereinigt mit Brennstoff-chemie, Bd. 40, Heft 12, December1987 * |
| FUEL, May 1980 volume 59, pages 290-294 * |
| Kirk-Othmer Encyclopedia of Chemical Technology, Volume 15 * |
| Trends in Petrochemical Technology, Chapter 3 Olefins Production pages 53-84 * |
Also Published As
| Publication number | Publication date |
|---|---|
| DE68903352T2 (de) | 1993-03-18 |
| DE68903352D1 (de) | 1992-12-10 |
| EP0337579A1 (de) | 1989-10-18 |
| ES2036022T3 (es) | 1993-05-01 |
| ATE82019T1 (de) | 1992-11-15 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US5421837A (en) | Process for manufacturing a solid fuel | |
| US4429172A (en) | Process for the production of modified pitches and low boiling aromatics and olefins and use of said pitches | |
| US5089114A (en) | Method for processing heavy crude oils | |
| US4045187A (en) | Carbonaceous material | |
| US1609097A (en) | Process of making charcoal briquettes and product derived therefrom | |
| US9567654B2 (en) | Binder for metallurgical coke and a process for making same | |
| EP0337579B1 (de) | Brikettbindemittel | |
| JPS6120599B2 (de) | ||
| US4135983A (en) | Method for improving coking property of coal for use in production of cokes | |
| JP2000256681A (ja) | 灯油及びその製造方法 | |
| US4243488A (en) | Coke compositions and process for manufacturing same | |
| US1929860A (en) | Process of producing fuel briquettes | |
| SU1055338A3 (ru) | Способ растворени угл | |
| HU206514B (en) | Process for producing benzine, gas-oil and heating oil from metal- and sulfur-containing petrol-rests | |
| GB2066285A (en) | Binder for coal briquettes | |
| JP4749183B2 (ja) | 強度増進特性に優れた粘結補填材と高強度コークスの製造方法 | |
| US2370060A (en) | Briquette and process of manufacturing same | |
| RU2144559C1 (ru) | Состав для получения топливных брикетов | |
| SU1048988A3 (ru) | Способ получени высокоароматического пекообразного продукта | |
| JP4936795B2 (ja) | 強度増進特性に優れた粘結補填材と高強度コークスの製造方法 | |
| GB2065696A (en) | Process for the coking quality of coals having unsatisfactory properties | |
| US5104417A (en) | Substitute coal from acetylene production by-products | |
| CS209517B2 (en) | Coal briquettes with decreased emission of solid substances | |
| GB2067590A (en) | Bituminous binder for making roads or other traffic-bearing surfaces | |
| RU2226541C2 (ru) | Способ получения битума |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
Free format text: ORIGINAL CODE: 0009012 |
|
| AK | Designated contracting states |
Kind code of ref document: A1 Designated state(s): AT BE CH DE ES FR GB GR IT LI LU NL SE |
|
| 17P | Request for examination filed |
Effective date: 19900404 |
|
| 17Q | First examination report despatched |
Effective date: 19901109 |
|
| RAP1 | Party data changed (applicant data changed or rights of an application transferred) |
Owner name: THE DOW CHEMICAL COMPANY |
|
| GRAA | (expected) grant |
Free format text: ORIGINAL CODE: 0009210 |
|
| AK | Designated contracting states |
Kind code of ref document: B1 Designated state(s): AT BE CH DE ES FR GB GR IT LI LU NL SE |
|
| PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: GR Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 19921104 |
|
| REF | Corresponds to: |
Ref document number: 82019 Country of ref document: AT Date of ref document: 19921115 Kind code of ref document: T |
|
| ET | Fr: translation filed | ||
| REF | Corresponds to: |
Ref document number: 68903352 Country of ref document: DE Date of ref document: 19921210 |
|
| ITF | It: translation for a ep patent filed | ||
| REG | Reference to a national code |
Ref country code: ES Ref legal event code: FG2A Ref document number: 2036022 Country of ref document: ES Kind code of ref document: T3 |
|
| PLBE | No opposition filed within time limit |
Free format text: ORIGINAL CODE: 0009261 |
|
| STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT |
|
| 26N | No opposition filed | ||
| EPTA | Lu: last paid annual fee | ||
| EAL | Se: european patent in force in sweden |
Ref document number: 89200939.0 |
|
| PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: FR Payment date: 19950212 Year of fee payment: 7 |
|
| PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: SE Payment date: 19950217 Year of fee payment: 7 |
|
| PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: CH Payment date: 19950220 Year of fee payment: 7 |
|
| PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: LU Payment date: 19950301 Year of fee payment: 7 |
|
| PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: BE Payment date: 19950306 Year of fee payment: 7 |
|
| PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: GB Payment date: 19950331 Year of fee payment: 7 |
|
| PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: AT Payment date: 19950403 Year of fee payment: 7 |
|
| PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: NL Payment date: 19950430 Year of fee payment: 7 |
|
| PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: DE Payment date: 19960311 Year of fee payment: 8 |
|
| PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: LU Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 19960414 Ref country code: GB Effective date: 19960414 Ref country code: AT Effective date: 19960414 |
|
| PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: SE Effective date: 19960415 |
|
| PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: LI Effective date: 19960430 Ref country code: CH Effective date: 19960430 Ref country code: BE Effective date: 19960430 |
|
| BERE | Be: lapsed |
Owner name: THE DOW CHEMICAL CY Effective date: 19960430 |
|
| PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: NL Effective date: 19961101 |
|
| GBPC | Gb: european patent ceased through non-payment of renewal fee |
Effective date: 19960414 |
|
| REG | Reference to a national code |
Ref country code: CH Ref legal event code: PL |
|
| PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: FR Effective date: 19961227 |
|
| NLV4 | Nl: lapsed or anulled due to non-payment of the annual fee |
Effective date: 19961101 |
|
| EUG | Se: european patent has lapsed |
Ref document number: 89200939.0 |
|
| REG | Reference to a national code |
Ref country code: FR Ref legal event code: ST |
|
| PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: ES Payment date: 19970411 Year of fee payment: 9 |
|
| PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: DE Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 19980101 |
|
| PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: ES Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 19980415 |
|
| REG | Reference to a national code |
Ref country code: ES Ref legal event code: FD2A Effective date: 20000403 |
|
| PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: IT Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES;WARNING: LAPSES OF ITALIAN PATENTS WITH EFFECTIVE DATE BEFORE 2007 MAY HAVE OCCURRED AT ANY TIME BEFORE 2007. THE CORRECT EFFECTIVE DATE MAY BE DIFFERENT FROM THE ONE RECORDED. Effective date: 20050414 |