PL89262B1 - - Google Patents
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- Publication number
- PL89262B1 PL89262B1 PL1973160970A PL16097073A PL89262B1 PL 89262 B1 PL89262 B1 PL 89262B1 PL 1973160970 A PL1973160970 A PL 1973160970A PL 16097073 A PL16097073 A PL 16097073A PL 89262 B1 PL89262 B1 PL 89262B1
- Authority
- PL
- Poland
- Prior art keywords
- tellurium
- titanium
- catalyst
- atomic ratio
- olefins
- Prior art date
Links
- 239000003054 catalyst Substances 0.000 claims description 19
- PORWMNRCUJJQNO-UHFFFAOYSA-N tellurium atom Chemical compound [Te] PORWMNRCUJJQNO-UHFFFAOYSA-N 0.000 claims description 15
- 229910052714 tellurium Inorganic materials 0.000 claims description 14
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 claims description 9
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 claims description 9
- 229910052719 titanium Inorganic materials 0.000 claims description 8
- 239000010936 titanium Substances 0.000 claims description 8
- 150000001336 alkenes Chemical class 0.000 claims description 7
- 238000000034 method Methods 0.000 claims description 7
- 230000003647 oxidation Effects 0.000 claims description 6
- 238000007254 oxidation reaction Methods 0.000 claims description 6
- 239000000203 mixture Substances 0.000 claims description 5
- FXADMRZICBQPQY-UHFFFAOYSA-N orthotelluric acid Chemical compound O[Te](O)(O)(O)(O)O FXADMRZICBQPQY-UHFFFAOYSA-N 0.000 claims description 4
- 150000002927 oxygen compounds Chemical class 0.000 claims description 3
- 238000002360 preparation method Methods 0.000 claims description 3
- 239000004408 titanium dioxide Substances 0.000 claims description 2
- XJDNKRIXUMDJCW-UHFFFAOYSA-J titanium tetrachloride Chemical compound Cl[Ti](Cl)(Cl)Cl XJDNKRIXUMDJCW-UHFFFAOYSA-J 0.000 claims description 2
- YONPGGFAJWQGJC-UHFFFAOYSA-K titanium(iii) chloride Chemical compound Cl[Ti](Cl)Cl YONPGGFAJWQGJC-UHFFFAOYSA-K 0.000 claims description 2
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 6
- 229910021529 ammonia Inorganic materials 0.000 description 5
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 5
- 239000001301 oxygen Substances 0.000 description 5
- 229910052760 oxygen Inorganic materials 0.000 description 5
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- 150000002825 nitriles Chemical class 0.000 description 4
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 4
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 description 4
- WEVYAHXRMPXWCK-UHFFFAOYSA-N Acetonitrile Chemical compound CC#N WEVYAHXRMPXWCK-UHFFFAOYSA-N 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- 239000002244 precipitate Substances 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- 238000003756 stirring Methods 0.000 description 3
- NLHHRLWOUZZQLW-UHFFFAOYSA-N Acrylonitrile Chemical compound C=CC#N NLHHRLWOUZZQLW-UHFFFAOYSA-N 0.000 description 2
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 2
- 150000001993 dienes Chemical class 0.000 description 2
- 229930195733 hydrocarbon Natural products 0.000 description 2
- LELOWRISYMNNSU-UHFFFAOYSA-N hydrogen cyanide Chemical compound N#C LELOWRISYMNNSU-UHFFFAOYSA-N 0.000 description 2
- 239000012265 solid product Substances 0.000 description 2
- LAJZODKXOMJMPK-UHFFFAOYSA-N tellurium dioxide Chemical compound O=[Te]=O LAJZODKXOMJMPK-UHFFFAOYSA-N 0.000 description 2
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 1
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- 229910017835 Sb—Sn Inorganic materials 0.000 description 1
- 229910003069 TeO2 Inorganic materials 0.000 description 1
- 229910010413 TiO 2 Inorganic materials 0.000 description 1
- 229910052770 Uranium Inorganic materials 0.000 description 1
- 238000002441 X-ray diffraction Methods 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 150000001299 aldehydes Chemical class 0.000 description 1
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 1
- 235000011114 ammonium hydroxide Nutrition 0.000 description 1
- 229910052787 antimony Inorganic materials 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 229910052797 bismuth Inorganic materials 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 238000001354 calcination Methods 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 238000004817 gas chromatography Methods 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- QJGQUHMNIGDVPM-UHFFFAOYSA-N nitrogen group Chemical group [N] QJGQUHMNIGDVPM-UHFFFAOYSA-N 0.000 description 1
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 description 1
- -1 olefin hydrocarbons Chemical class 0.000 description 1
- 150000002926 oxygen Chemical class 0.000 description 1
- 230000000737 periodic effect Effects 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000010992 reflux Methods 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- XHGGEBRKUWZHEK-UHFFFAOYSA-L tellurate Chemical compound [O-][Te]([O-])(=O)=O XHGGEBRKUWZHEK-UHFFFAOYSA-L 0.000 description 1
- 150000003498 tellurium compounds Chemical class 0.000 description 1
- OGIDPMRJRNCKJF-UHFFFAOYSA-N titanium oxide Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C253/00—Preparation of carboxylic acid nitriles
- C07C253/24—Preparation of carboxylic acid nitriles by ammoxidation of hydrocarbons or substituted hydrocarbons
- C07C253/26—Preparation of carboxylic acid nitriles by ammoxidation of hydrocarbons or substituted hydrocarbons containing carbon-to-carbon multiple bonds, e.g. unsaturated aldehydes
-
- 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
- B01J27/00—Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
- B01J27/02—Sulfur, selenium or tellurium; Compounds thereof
- B01J27/057—Selenium or tellurium; Compounds thereof
- B01J27/0576—Tellurium; Compounds thereof
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C45/00—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds
- C07C45/27—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by oxidation
- C07C45/32—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by oxidation with molecular oxygen
- C07C45/33—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by oxidation with molecular oxygen of CHx-moieties
- C07C45/34—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by oxidation with molecular oxygen of CHx-moieties in unsaturated compounds
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C45/00—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds
- C07C45/27—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by oxidation
- C07C45/32—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by oxidation with molecular oxygen
- C07C45/33—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by oxidation with molecular oxygen of CHx-moieties
- C07C45/34—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by oxidation with molecular oxygen of CHx-moieties in unsaturated compounds
- C07C45/35—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by oxidation with molecular oxygen of CHx-moieties in unsaturated compounds in propene or isobutene
-
- 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
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/52—Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Catalysts (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Description
Przedmiotem wynalazku jest katalizator procesu utleniania lub amoutleniania weglowodorów olefi- nowych i sposób jego wytwarzania.Ze znanych katalizatorów procesu utleniania lub amoutleniania olefin najwazniejsze sa tlenowe zwiazki co najmniej dwóch pierwiastków, zwlasz¬ cza Mo-Bi, Sb-U, Sb-Sn lub Sb-Fe.Z opisu patentowego Stanów Zjednoczonych Ameryki nr 3164627 wiadomo, ze tlenowe zwiazki telluru mozna stosowac w procesach wytwarzania nienasyconych nitryli przez amoutlenianie olefin, to jest przez dzialanie na olefiny gazem zawiera¬ jacym tlen i amoniak, zas z opisu patentowego Stanów Zjednoczonych Ameryki nr 3164626 znane jest stosowanie telluru zmieszanego z tlenkami in¬ nych piarwiastków jako katalizatora procesu amo- , utleniania.Znane katalizatory zawierajace tellur umozli¬ wiaja wprawdzie selektywna synteze akrylonitrylu z propylenu, amoniaku i tlenu, ale wada ich jest to, ze reakcje prowadzone w ich obecnosci prze¬ biegaja tak silnie egzotermicznie, ze trudno jest regulowac ich przebieg, a poza tym w celu otrzy¬ mania nitryli z dobra wydajnoscia trzeba stosowac duze ilosci amoniaku, poniewaz liczne katalizatory tego typu powoduja powstawanie znacznych ilosci produktów ubocznych zawierajacych azot, takich jak kwas cyjanowodorowy i acetonitryl. Wada tych katalizatorów jest równiez to, ze stosunkowo szybko ulegaja dezaktywacji, a regeneracja ich jest kosztowna, zas samo ich wytwarzanie jest dosc skomplikowane. Katalizator wedlug wynalaz¬ ku nie ma tych wad i umozliwia proste i nie kosz¬ towne przetwarzanie weglowodorów olefinowych w nienasycone nitryle lub aldehydy albo sprzezo¬ ne dieny.Katalizator wedlug wynalazku stanowi miesza¬ nine zwiazków tytanu i telluru zawierajacych tlen, przy czym stosunek ilosci atomów telluru do ilosci atomów tytanu w tych zwiazkach wynosi 10 :1— 1 : 5. Szczególnie korzystne wlasciwosci ma kata¬ lizator, który jak wykazuje analiza rentgenowska, zawiera telluran tytanu TiTe308. Katalizator wed¬ lug wynalazku moze oprócz mieszaniny o wyzej podanym skladzie, zawierac jeden lub wieksza liczbe innych pierwiastków, zwlaszcza pierwiast¬ ków nalezacych do V grupy okresowego ukladu pierwiastków, na przyklad fosforu. Ilosc dodanego pierwiastka, w stosunku atomowym do sumy ato¬ mów tytanu i telluru nie powinna byc wyzsza niz 1 : 5.Katalizator wedlug wynalazku wytwarza sie ze znanych produktów wyjsciowych, a sposób jego wytwarzania zalezy od rodzaju uzytych surowców i obejmuje takie zabiegi jak stracanie, saczenie, suszenie, rozdrabnianie, wyprazanie, wytlaczanie i tabletkowanie. Jako produkty wyjsciowe korzyst¬ nie jest stosowac metaliczny tellur, dwutlenek telluru Te02, kwasy tellurowe H2Te04 i H6Te06, które poddaje sie reakcji z dwutlenkiem tytanu 89 2623 {rutyl lub anataz), trójchlorkiem tytanu lub czte¬ rochlorkiem tytanu, przy czym ilosci reagentów dobiera sie tak, aby stosunek atomowy tytanu do telluru w katalizatorze wynosil 10 :1—1 :5, ko¬ rzystnie 5 :1—1 : 3, Katalizator wedlug wynalazku stosuje sie w po¬ staci zloza stalego lub fluidalnego w procesach wy¬ twarzania nitryli, pochodnych tlenowych lub sprze¬ zonych dienów na drodze utleniania lub amoutle^ niania olefin. Prace prowadzi sie przez dzialanie tlenu lub gazu zawierajacego tlen, zmieszanego ewentualnie z amoniakiem, na olefiny, korzystnie na propylen lub lzobutylen, nawet o mniejszym stopniu czystosci.Wynalazek jest dokladniej przedstawiony w lpo- niiszxch przyKfadach.Przyklad I. 50 g kwasu tellurowego HsTeC^ rozfnttAwfiAo^jf ^OOml wody, mieszajac ogrzewano do 'wrzenia 1 powoli (dodano 4 g Ti02 o wielkosci ziarn ponizej 20 mikronów, po czym odparowano mieszajac. Staly produkt umieszczono w mufli i wyprazano w obecnosci powietrza w temperatu¬ rze 530°C [w ciagu 5 godzin, nastepnie mielono i przesiano, gromadzac produkt o rozdrobnieniu 50—100 mesh. 6 ml otrzymanego katalizatora umieszczono w rurowym mikroreaktorze, ogrzewa¬ no w piecu elektrycznym do temperatury 470°C i fw ciagu 1 godziny wprowadzono do reaktora 75 ml propylenu, 100 ml amoniaku, 800 ml powie¬ trza i 750 ml pary wodnej. Objetosc tych gazów mierzono w temperaturze pokojowej, pod cisnie¬ niem atmosferycznym. Produkty reakcji analizowa¬ no metoda chromatografii gazowej, pobierajac próbki z dolu reaktora. Stopien przemiany propy¬ lenu wynosil 50%, a selektywnosc procesu wytwa¬ rzania akrylonitrylu wynosila 63%.Przykfad II. [Do 53 g 15% roztworu TiCl« do¬ dano 30 ml 30% roztworu NH4OH i 120 objetosci nadtlenku wodoru. Po odstaniu sie osadu zdekan- towano ciecz, osad odsaczono i trzykrotnie prze¬ myto iwoda. Oddzielnie rozpuszczono 5 g H2Te04 w 100 ml wody i do otrzymanego roztworu dodano 1262 4 osad otrzymany w sposób wyzej opisany, zmiesza¬ no i odparowano ogrzewajac. Staly produkt wy¬ prazono w strumieniu powietrza w temperaturze 520°C w ciagu 8 godzin a otrzymany katalizator zmielono i przesiano, gromadzac frakcje o rozdrob¬ nieniu 50—100 mesh.Przyklad III. 23 g kwasu tellurowego roz¬ puszczono w 100 ml wody, dodano 2,3 g 86% kwa- io su fosforowego i nastepnie 18 g TiO*. Postepowa¬ no |dalej w sposób opisany w przykladzie II.Przyklad IV. 42 g sproszkowanego metalicz¬ nego telluru zmieszano z woda, zawiesine ogrze- i, wano do temperatury okolo 100°C i powoli dodano * 120 objetosci nadtlenku wodoru, w celu przepro- ) wadzenia telluru w kwas tellurowy w postaci roz¬ tworu. Nastepnie do roztworu dodano stopniowo 80 g sproszkowanego Ti02 (anataz), ogrzewano i odparowano, po czym wyprazono w powietrzu w temperaturze 55°C w ciagu 4 godzin, a otrzyma¬ ny katalizator zmielono i przesiano, gromadzac frakcje o rozdrobnieniu 50—100 mesh. PL
Claims (3)
- Zastrzezenia patentowe 1. Katalizator procesu utleniania lub amoutlenia- nia olefin, znamienny tynujse stanowi mieszanine tlenowych zwiazków telluru i tytanu, w której ^ stosunek atomowy telluru do tytanu wynosi 10 :1—1 : 5.
- 2. Katalizator wedlug zastrz. 1, znamienny tym, ze zawiera tellur i tytan w stosunku atomowym 33 5:1—1 :3.
- 3. Sposób wytwarzania katalizatora procesu utleniania lub amoutleniania olefin, znamienny tym, ze metaliczny tellur, tlenek telluru lub kwas 40 tellurowy poddaje sie reakcji z dwutlenkiem ty¬ tanu, trójchlorkiem tytanu lub czterochlorkiem ty¬ tanu, w stosunku atomowym telluru do tytanu wynoszacym od 10:1 do 1:5, korzystnie od 5:1 do 1 :3. RSW Zakl. Graf. W-wa, Srebrna 16, z. 63-77/0 Cena 10 zl — 110 egz. PL
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
IT21249/72A IT949753B (it) | 1972-03-01 | 1972-03-01 | Catalizzatori di ossidazione e di ammonossidazione loro procedimen to di preparazione e loro impieghi |
Publications (1)
Publication Number | Publication Date |
---|---|
PL89262B1 true PL89262B1 (pl) | 1976-11-30 |
Family
ID=11179012
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PL1973160970A PL89262B1 (pl) | 1972-03-01 | 1973-02-28 |
Country Status (26)
Country | Link |
---|---|
JP (1) | JPS5410943B2 (pl) |
AR (1) | AR200009A1 (pl) |
AT (1) | AT325591B (pl) |
AU (1) | AU469131B2 (pl) |
BE (1) | BE795920A (pl) |
BG (1) | BG23747A3 (pl) |
BR (1) | BR7301577D0 (pl) |
CA (1) | CA992561A (pl) |
CH (2) | CH584176A5 (pl) |
CS (2) | CS183676B2 (pl) |
DD (1) | DD106368A5 (pl) |
DE (1) | DE2310330A1 (pl) |
ES (1) | ES412313A1 (pl) |
FR (1) | FR2174115A1 (pl) |
GB (1) | GB1408800A (pl) |
HU (1) | HU165435B (pl) |
IE (1) | IE37484B1 (pl) |
IT (1) | IT949753B (pl) |
LU (1) | LU67119A1 (pl) |
NL (1) | NL7302846A (pl) |
PL (1) | PL89262B1 (pl) |
RO (1) | RO62271A (pl) |
SU (2) | SU513619A3 (pl) |
TR (1) | TR17436A (pl) |
ZA (1) | ZA731241B (pl) |
ZM (1) | ZM3373A1 (pl) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4704375A (en) * | 1986-05-19 | 1987-11-03 | Intevep, S.A. | Vanadium passivating agent for use in a cracking catalyst |
KR20200038014A (ko) * | 2018-10-02 | 2020-04-10 | 주식회사 케이씨텍 | 표면처리 조성물 및 그것을 이용한 표면처리 방법 |
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1972
- 1972-03-01 IT IT21249/72A patent/IT949753B/it active
-
1973
- 1973-02-21 ZA ZA731241A patent/ZA731241B/xx unknown
- 1973-02-22 AU AU52475/73A patent/AU469131B2/en not_active Expired
- 1973-02-26 AR AR246808A patent/AR200009A1/es active
- 1973-02-26 CH CH1467075A patent/CH584176A5/xx not_active IP Right Cessation
- 1973-02-26 BE BE795920D patent/BE795920A/xx unknown
- 1973-02-26 IE IE290/73A patent/IE37484B1/xx unknown
- 1973-02-26 CH CH278873A patent/CH575778A5/xx not_active IP Right Cessation
- 1973-02-26 ES ES412313A patent/ES412313A1/es not_active Expired
- 1973-02-27 TR TR17436A patent/TR17436A/xx unknown
- 1973-02-27 GB GB964373A patent/GB1408800A/en not_active Expired
- 1973-02-28 LU LU67119A patent/LU67119A1/xx unknown
- 1973-02-28 SU SU1890213A patent/SU513619A3/ru active
- 1973-02-28 SU SU1957936A patent/SU482035A3/ru active
- 1973-02-28 DD DD169657A patent/DD106368A5/xx unknown
- 1973-02-28 HU HUSA2467A patent/HU165435B/hu unknown
- 1973-02-28 NL NL7302846A patent/NL7302846A/xx not_active Application Discontinuation
- 1973-02-28 CS CS7300001446A patent/CS183676B2/cs unknown
- 1973-02-28 CS CS7600008286A patent/CS183699B2/cs unknown
- 1973-02-28 CA CA164,853A patent/CA992561A/en not_active Expired
- 1973-02-28 PL PL1973160970A patent/PL89262B1/pl unknown
- 1973-02-28 BG BG024520A patent/BG23747A3/xx unknown
- 1973-02-28 FR FR7307008A patent/FR2174115A1/fr not_active Withdrawn
- 1973-03-01 DE DE19732310330 patent/DE2310330A1/de active Pending
- 1973-03-01 AT AT186673A patent/AT325591B/de not_active IP Right Cessation
- 1973-03-01 BR BR731577A patent/BR7301577D0/pt unknown
- 1973-03-01 JP JP2378573A patent/JPS5410943B2/ja not_active Expired
- 1973-03-01 RO RO74040A patent/RO62271A/ro unknown
- 1973-03-01 ZM ZM33/73*UA patent/ZM3373A1/xx unknown
Also Published As
Publication number | Publication date |
---|---|
AT325591B (de) | 1975-10-27 |
CS183676B2 (en) | 1978-07-31 |
IE37484B1 (en) | 1977-08-03 |
DD106368A5 (pl) | 1974-06-12 |
CH575778A5 (pl) | 1976-05-31 |
AR200009A1 (es) | 1974-10-15 |
HU165435B (pl) | 1974-08-28 |
ZA731241B (en) | 1973-11-28 |
SU513619A3 (ru) | 1976-05-05 |
ATA186673A (de) | 1975-01-15 |
ES412313A1 (es) | 1976-05-01 |
BR7301577D0 (pt) | 1974-09-24 |
SU482035A3 (ru) | 1975-08-25 |
BG23747A3 (bg) | 1977-10-12 |
ZM3373A1 (en) | 1974-02-21 |
CH584176A5 (pl) | 1977-01-31 |
TR17436A (tr) | 1975-07-23 |
JPS5410943B2 (pl) | 1979-05-10 |
CS183699B2 (en) | 1978-07-31 |
DE2310330A1 (de) | 1973-09-20 |
NL7302846A (pl) | 1973-09-04 |
RO62271A (pl) | 1977-08-15 |
JPS48101390A (pl) | 1973-12-20 |
IT949753B (it) | 1973-06-11 |
IE37484L (en) | 1973-09-01 |
FR2174115A1 (pl) | 1973-10-12 |
LU67119A1 (pl) | 1973-05-03 |
GB1408800A (en) | 1975-10-08 |
AU5247573A (en) | 1974-08-22 |
CA992561A (en) | 1976-07-06 |
BE795920A (fr) | 1973-06-18 |
AU469131B2 (en) | 1976-02-05 |
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