GB2125390A - Preparation of zeolites - Google Patents
Preparation of zeolites Download PDFInfo
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- GB2125390A GB2125390A GB08321325A GB8321325A GB2125390A GB 2125390 A GB2125390 A GB 2125390A GB 08321325 A GB08321325 A GB 08321325A GB 8321325 A GB8321325 A GB 8321325A GB 2125390 A GB2125390 A GB 2125390A
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B33/00—Silicon; Compounds thereof
- C01B33/20—Silicates
- C01B33/26—Aluminium-containing silicates, i.e. silico-aluminates
- C01B33/28—Base exchange silicates, e.g. zeolites
- C01B33/2807—Zeolitic silicoaluminates with a tridimensional crystalline structure possessing molecular sieve properties; Isomorphous compounds wherein a part of the aluminium ore of the silicon present may be replaced by other elements such as gallium, germanium, phosphorus; Preparation of zeolitic molecular sieves from molecular sieves of another type or from preformed reacting mixtures
- C01B33/2876—Zeolitic silicoaluminates with a tridimensional crystalline structure possessing molecular sieve properties; Isomorphous compounds wherein a part of the aluminium ore of the silicon present may be replaced by other elements such as gallium, germanium, phosphorus; Preparation of zeolitic molecular sieves from molecular sieves of another type or from preformed reacting mixtures from a reacting mixture containing an amine or an organic cation, e.g. a quaternary onium cation-ammonium, phosphonium, stibonium
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B33/00—Silicon; Compounds thereof
- C01B33/20—Silicates
- C01B33/36—Silicates having base-exchange properties but not having molecular sieve properties
- C01B33/38—Layered base-exchange silicates, e.g. clays, micas or alkali metal silicates of kenyaite or magadiite type
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B39/00—Compounds having molecular sieve and base-exchange properties, e.g. crystalline zeolites; Their preparation; After-treatment, e.g. ion-exchange or dealumination
- C01B39/02—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof; Direct preparation thereof; Preparation thereof starting from a reaction mixture containing a crystalline zeolite of another type, or from preformed reactants; After-treatment thereof
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- Inorganic Chemistry (AREA)
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- Chemical Kinetics & Catalysis (AREA)
- Materials Engineering (AREA)
- Silicates, Zeolites, And Molecular Sieves (AREA)
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Abstract
A method of preparation of aluminosilicate zeolites is described in which the source of silicon in the reaction is, at least in part, a layer silicate especially magadiite or kenyaite.
Description
SPECIFICATION
Preparation of zeolites
The present invention relates to a method for the preparation of zeolites.
Zeolites have been known for very many years but interest in their use as molecular sieves and as catalysts has increased very considerably over the last 30 years. Many zeolites occur in nature and in recent years many synthetic zeolites have also been prepared. The technical literature of the last 25 years or so is replete with descriptions of new zeolites and of their preparation and with proposals for the use of zeolites, both old and new, as catalysts in a wide variety of chemical processes. Many of these proposals relate to the use of zeolites in processes used in the oil and petrochemical industry such as aromatisation, hydrocarbon cracking, isomerisation processes and the like.
Zeolites, both natural and synthetic, include a considerable number of cation-containing crystalline aluminosilicates which can be characterised as rigid three-dimensional frameworks of SiO4 and AlO4 in which the tetrahedra are cross-linked by the sharing of oxygen atoms whereby the ratio of the total aluminium and silicon atoms to oxygen is 1:2. The electrovalence of the tetrahedra containing aluminium is balanced by the inclusion in the crystal of a suitable cation. The properties of a given cation-containing aluminosilicate zeolite can be varied by suitable selection of a cation and it is now common practice to ion-exchange one cation for another, either partially or completely, so as to obtain a zeolite most suited for the particular purpose in mind.
Natural zeolites have generally been given generic names, for example faujasite, mordenite, while synthetic zeolites are usually designated by letters or other convenient symbols, for example zeolites A,
X, Y, FU-1, NU-1, ZSM-5 etc.
A considerable amount of attention has been paid to the preparation of synthetic zeolites with such objects in view as cheaper routes to zeolites and the preparation of purer forms of the zeolites.
Since zeolites are aluminosilicates, starting materials for their preparation must include at least sources of aluminium and of silicon. Many such sources have been proposed from among the many compounds of these elements including for example various metal silicates, metal aluminates, silica, aluminium hydroxide and also compounds which can serve as sources of both silicon and aluminium.
According to the present invention a method for preparing a crystalline aluminosilicate zeolite comprises forming a reaction mixture comprising at least one source of aluminium and at least one source of silicon and crystallising the zeolite from the reaction mixture characterised in that the source of silicon comprises, at least in part, a layer silicate. Layer silicates have been extensively described in the technical literature. For example, Eugster in Science 157 (1967) P. 1177 describes some layered sodium silicates. Silicate sheet structures are discussed by Breck in his book "Zeolite Molecular
Sieves" (Wiley-lnterscience 1974) at page 35, examples of such sheet structures being kaolinate, montmorillonite clays, micas and some zeolites, for example heulandite.Further descriptions of layer silicates appear in "Crystal Structures of Clay Minerals and their X-ray Identification", Monograph No.
5 of the Mineralogical Society Ed. G. W. Brindley and G. Brown (1980) pages 2 and 380.
Preferably, the layer silicate comprises magadiite or kenyaite in either natural or synthetic form.
The Applicants have found that magadiite is a particularly attractive source of silicon as it enables useful zeolites to be prepared both cheaply and easily. A further advantage of the use of magadiite and kenyaite is their low content of aluminium. A prime source of natural magadiite is the area in East
Africa around Lake Magadi. The exact structure of magadiite is not known but synthetic magadiite is known to have the molecular formula Na2Si14O29. 1 2H2O. Natural magadiite is known to contain small amounts of potassium, calcium and iron and X-ray diffraction also shows the presence of an anorthoclase type material (Ca, K, Na)AlSi3O8.
In preferred embodiments of the present invention the reaction mixture comprises at least one source of aluminium, magadiite as the source, at least in part, of silicon, and an organic material.
Preferably the organic material is a quaternary ammonium cation, more preferably a quaternary alkylammonium cation, for example tetrapropyl ammonium.
Examples
The syntheses hereinafter described were carried out in 1000 or 300 cm3 stainless steel autoclaves equipped with "Magnadrive" turbine stirrers. The autoclaves were cleaned prior to each synthesis by heating 1 M sodium hydroxide solution in them for 16 hours at 1 600 C.
Synthetic magadiite was made by a modification of a route described by Lagaly et al in Z.
Naturforsch (1973), 286, 234. Two separate syntheses, A and B, were carried out from different sources of silicon. In each synthesis, however, the molar composition of the reaction mixture was
NaOH, 3.51 SiO2, 37.5 H2O.
Synthesis A
A solution of sodium hydroxide (24g) in deionised water (405g) was added to silica gel ( 1 62g, analysed as 2.3 Na2O,AI2O3,2321 SiO2, 2163 H20) and the mixture reacted under autogeneous pressure in a 1 litre autoclave at 1 200C for 137 hours with stirring at 600 rpm. After cooling to room temperature, the product was filtered, washed with deionised water until neutral and then dried at 1 000C for 1 6 hours. The yield of sodium magadiite was 1249. The powder X-ray diffraction data are recorded in Table 1 and were assigned as sodium magadiite. Elemental analysis of the product gave 4.8 wt% Na,38.1 wt% Si and 10.1 wt% H2O.
Table 1
Relative
d(A) intensity I/Io d(A) I/lo
15.56 100 3.31 58
7.76 12 3.15 61
7.26 3 2.82 5
5.18 18 2.63 3
3.87 2 2.42 2
3.55 29 2.35 5
3.45 94 2.22 3
2.06 2
Synthesis B
A solution of sodium hydroxide (24g) in deionised water (96g) was added with stirring to "Syton"
X 30 colloidal silica (438.89, analysis 27 Na2O, Al203, 2400 SiO2, 19,550 H20) in a 1 litre autoclave.
The mixture was reacted under autogeneous pressure at 1 200C for 120 hours with stirring at 500 r.p.m. After cooling to room temperature, the product was filtered, washed with deionised water until neutral and then dried at 1 000C for 16 hours. The yield of sodium magadiite was 110g. The X-ray diffraction data were assigned as those of sodium magadiite and are shown in Table 2. Elemental analysis of the product gave: 5.2 wt% Na, 35.5 wt% Si and 9.0 wt% H20 Table 2
d(A) I/Io d(A) I/IO
15.45 90 3.45 100
11.11 2 3.31 64
7.76 9 3.15 66
7.26 3 2.83 5
5.18 19 2.63 3
4.44 0 2.59 7
3.89 0 2.35 3
3.64 22 2.30 3
3.56 31 2.06 2
Natural magadiite
Natural magadiite was obtained from the Magadi Soda Company, Kenya. The as-supplied material was ground, washed with denionised water and dried at 100 C for 16 hours. The X-ray powder diffraction pattern was assigned as sodium magadiite with some anorthoclase and calcite impurities and is shown in Table 3. The analysis of the material was (in terms of mole ratios): 0.4 K20: 0.5 CaO: 0.4 Fe203: 2.8 Na20: Al2O3: 33.6 SiO2: 1 2H20.
Elemental analysis gave (all percentages in wt%). 1.0% K,4.3% A, 0.7% Ca, 1.5% Fe, 1.8% Al, 31.4% Si and 7.3% HzO.
Table 3 d(A) 1/I0 d(A) I/lo
15.51 100 3.30 43
10.51 0 3.24 26(A)
8.48 1 3.21 30(A)
7.77 11 3.14 45
7.25 2 3.03 11
6.86 2 3.00 10
6.48 2(A) 2.87 10
5.63 4 2.82 7
5.18 19 2.74 5
5.02 14 2.64 4
4.69 5 2.59 8
4.47 21 2.54 6(C)(A)
4.10 7(A) 2.41 2
4.02 12 2.35 6
3.90 10(C) 2.28 4(C)
3.75 8(A) 2.16 1(A)
3.62 15 2.09 1(C) 3.55 20 2.07 1
3.44 63 2.01 1
Key: (A) Analcime
(C) Calcite
Example 1
Preparation of zeolite ZSM-5
A solution of sodium aluminate (1.36g, analysis 1.22 Na2O, Al2O3,1.02 H2O) and sodium hydroxide (4.689) in deionised water (609) was added with stirring to a suspension of sodium magadiite (29.2g-prepared as in Synthesis A) in a 1 litre stainless steel autoclave.The mixture was reacted at 1 500C under autogeneous pressure for 11 7 hours. The mixture was then cooled to room temperature, tetrapropylbromide added (13.729), and the mixture again reacted under autogeneous pressure at 1 500C for a further 89 hours with stirring at 500 r.p.m. After cooling to room temperature, the product was filtered, washed with deionised water and dried at 1 000C for 3 hours. The yield was 20g.
The powder X-ray diffraction pattern was consistent with a mixture of ZSM-5 type zeolite (with a pronounced orientation effect in the intensity of the peak at a d-spacing of 1 0A) with ct-quartz and some mordenite. Normal intensities were observed after wet grinding. The X-ray diffraction pattern is shown in Table 4. The ZSM-5 type zeolite had a silica/alumina mole ratio of 40. Elemental analysis gave (all percentages in wt%): 4.99% C,1.41 H, 0.47% N, 1.76% Na,39.6% Si,1.9% Al.
Table 4
d(AJ l/lo d(A) 1/lO d(A) I/lo
13.81 3(M) 5.02 26* 3.00 7
11.32 8 4.64 4 2.96 5
10.10 93* 4.55 6(M) 2.90 5
9.85 4 4.49 3 2.80 1
9.16 9(M) 4.39 3 2.74 3
7.52 5 4.29 15(Q) 2.70 1
7.15 4 4.02 13 2.62 4
6.77 3 3.85 100 2.57 2
6.64 5 3.78 37 2.52 5
6.43 6(M) 3.74 20 2.50 8
6.11 4 3.67 16 2.47 5
6.04 5(M) 3.49 19(M) 2.41 2
5.77 7 3.36 79(Q) 2.34 1
5.61 5 3.22 9(M) 2.29 5
5.42 1 3.16 2 2.25 2
5.17 2 3.07 8 2.21 1 Key: (Q) a -quartz (M) mordenite-type catalyst
* pronounced orientation effect
Example 2 Example 1 was repeated except that in the initial reaction mixture the amounts of reactants were sodium aluminate (1.36g), sodium hydroxide (2.2g) in deionised water (609) and added to sodium magadiite (29.2g from Synthesis A) in deionised water (297g). The reaction mixture was cooled to room temperature after 114 hours and tetrapropylammonium bromide (13729) added. Thereafter the mixture wa. reacted under autogeneous pressure at 1 500C for 89 hours with stirring at 500 r.p.m.
After cooling 3 to room temperature, the product was filtered, washed with deionised water until neutral and dried at 1 000C for 3 hours. The yield of product was 1 7g. The powder X-ray diffraction pattern was consis nt with a ZSM-5 type zeolite and is recorded in Table 5. The ZSM-5 type zeolite had a silica/alumina ratio of 45. Elemental analysis of the product showed (all percentages by weight): 6.58% C, 1.78% H, 0.62% N,1.68% Na, 39.5% Si, 1.7% Al.
Table 5
d(A) 1/Io d(A) I/lo d(A) I/lo
13.62 2(M) 5.57 4 3.76 36
11.17 9 5.38 1 3.72 18 10.00 30 5.14 2 3.65 14
9.06 7(M) 5.00 8 3.47 14(M)
7.45 4 4.87 0 3.44 9
7.09 3 4.61 4 3.39 10(M)
6.71 3 4.52 5(M) 3.34 8
6.58 4 4.45 2 3.24 7
6.38 5(M) 4.37 3 3.20 8(M)
6.07 4 4.27 6 3.14 2
6.00 5(M) 4.00 13
5.73 6 3.83 100 ty: (M)-mordenite-type zeolite
Example 3 Exams e 1 was repeated except that:
(a) the tetrapropylammonium bromide was added at the start of the synthesis
(b) thee was therefore no intermediate cooling
(c) thc otal reaction time was 72 hours.
The yilid of product was 1 89 and its X-ray diffraction pattern was consistent with sodium tetra propylammcnium ZSM-5 type zeolite. The X-ray pattern is recorded in Table 6. The ZSM-5 type zeolite had a silica/ lumina mole ratio of 45 and the elemental analysis was (all percentages by weight): 7.27% C. 1.82% H, 0.68% N,1.38% Na, 39.7% Si, 1.7% Al.
Table 6 d(A) 1/i0 d(A) 1/l0 d(A) 1/l0
13.60 1(M) 5.57 5 3.84 100
11.17 11 5.38 1 3.76 36
10.00 25 5.14 2 3.72 22
9.05 4(M) 5.00 7 3.65 17
7.45 5 4.61 4 3.47 11(M)
7.09 3 4.52 3(M) 3.44 9
6.69 2 4.47 3 3.39 7(M) 6.58. 3 4.37 4 3.33 8
6.38 4(M) 4.27 6 3.24 5
6.00 5(M) 4.09 1 3.20 6(M)
5.72 6 4.00 10 3.42 2
Key: (M)-mordenite-type zeolite
Example 4
A solution of sodium aluminate (0.3229), sodium hydroxide (1.169) and tetrapropylammonium bromide (3.27g) in deionized water (779) was added to synthetic sodium magadiite (6.0g from
Synthesis B) in a 300 cm3 stainless steel autoclave. The mixture was reacted under autogeneous pressure at 1 500C for 94 hours with stirring at 500 r.p.m.After cooling to room temperature the product was filtered, washed with deionized water until neutral and dried at 1 000C for 16 hours. The yield of product was 2.7g. Its X-ray diffraction pattern, which is recorded in Table 7, was consistent with sodium tetrapropylammonium ZSM-5 type zeolite. The zeolite had a silica/alumina mole ratio of 39 and its elemental analysis (all percentages by weight) was: 7.34% C, 1.73% H,0.65% N, 38.6% Si,
1.9% Al.
Table 7 d(A) 1/Io d(A) 1/Io d(A) I/lo
13.62 1(M) 5.58 7 3.84 100
11.18 12 5.38 1 3.76 36
10.02 26 5.14 2 3.72 22
9.06 5(M) 5.00 7 3.66 18
8.06 0 4.85 1 3.47 11(M)
7.46 5 4.61 4 3.44 10
7.10 3 4.52 3(M) 3.39 8(M)
6.70 2 4.47 3 3.33 8
6.52 3 4.37 4 3.24 5
6.38 5(M) 4.27 7 3.20 6(M)
6.01 5(M) 4.09 2 3.15 2
5.73 6 4.01 10
Key: (M)-mordenite-type zeolite
Example 5
A solution of sodium aluminate (0.4g), sodium hydroxide (1.58g) and tetrapropylammonium bromide (4.19) in deionised water (108g) was added to synthetic sodium magadiite (6.0g from
Synthesis B) in a 300 cm3 stainless steel autoclave. The mixture was reacted under autogeneous pressure at 1 500C for 114 hours with stirring at 500 r.p.m.After cooling to room temperature, the product was filtered, washed with deionised water until neutral and dried at 1 000C for 3 hours. The yield of product was 1 .9g and the product powder X-ray diffraction pattern was consistent with a mixture of ZSM-5 type zeolite and an analcime (P-C type) zeolite. The diffraction pattern is recorded in
Table 8. The ZSM-5 type zeolite had a silica/alumina mole ratio of 23:1. Elemental analysis of the product (all percentages by weight) gave: 5.46% C, 1.48% H, 0.46% N, 3.6% Na, 37.6% Si and 3.1% Al.
Table 8
d(A) Mlo d(A) Ulo d(A) 1/10
11.23 9 4.62 3 3.19 3
10.04 27 4.47 3 3.14 1
9.04 2 4.38 3 3.06 10
7.48 5 4.28 7 2.99 8
7.11 3 4.09 1 2.95 6
6.73 1 4.02 6 2.92 25(A)
6.39 3 3.84 100 2.79 3(A)
6.01 5 3.77 39 2.74 2
5.72 9. 3.73 20 2.68 8(A)
5.59 41 (A) 3.66 17 2.62 4
5.40 1 3.60 2 2.58 2
5.15 2 3.42 59(A) 2.52 3
5.01 9 3.34 8
4.84 6(A) 3.26 3
Key: (A)-analcime (P-C type) zeolite
Example 6
A solution of sodium aluminate (0.789) sodium hydroxide (2.719) and tetrapropylammonium bromide (8.069) in deionised water (1009) was added to natural magadiite (209) in deionised water (11 2g) in a 1 litre stainless steel autoclave.The mixture was reacted under autogeneous pressure for 65 hours at 1 500C with stirring at 500 r.p.m. After cooling to room temperature, the product was filtered, washed with deionised water until neutral and dried at 1 000C for 16 hours. The yield of product was 14.79. The powder X-ray diffraction pattern of the product is recorded in Table 9 and is consistent with a mixture of ZSM-5 type zeolite and anorthoclase. The ZSM-5 type zeolite had a silica/alumina molar ratio of 28:1. A trace of mordenite was also present in the product. The elemental analysis of the product (all percentages by weight) was: 5.17% C,1.47% H,0.47% N, 2.2% A, 0.8% K, 0.5% Ca,35.3% Si, 2.4% Al, 1.3% Fe.
Table 9
d(A) 1/lo d(A) I/lo d(A) 1/lo
13.62 2(M) 5.38 1 3.47 17(M)
11.19 14 5.14 2 3.44 14
10.03 23 5.00 5 3.39 11(M)
9.73 5 4.61 5 3.34 11
9.07 7(M) 4.52 6(M) 3.24 16(A)
8.52 1 4.46 4 3.21 16(A)(M)
7.46 5 4.37 5 3.14 1
7.10 3 4.27 8 3.06 10
6.70 3 4.10 3(A) 2.99 11
6.56 5 4.00 13(M) 2.95 7
6.39 7(M) 3.84 100 2.90 5
6.03 6(M) 3.76 38(A) 2.79 1
5.73 7 3.73 28(A) 2.74 3
5.58 7 3.65 20 2.69 1
Key: (A)-anorthoclase (M)-mordenite-type zeolite
Example 7
Example 6 was repeated except that:
(a) no sodium aluminate was used, and
(b) total reaction time was 94 hours.
The yield of product was 139 and its powder X-ray diffraction pattern, which is recorded in Table 10, is consistent with a ZSM-5 type zeolite. The silica/alumina mole ratio of the product was 58 and its elemental analysis (all percentages by weight) was: 7.52% C,1.85% H,0.73% N, 0.6% Na,0.2% K, 0.5% Ca,38.9% Si, 1.3% Al, 1.3% Fe.
Table 10
d(A) Ulo d(A) 1/lo d(A) Iflo 11.19 16 5.38 1 3.72 31
10.03 20 5.14 2 3.65 23
9.73 6 5.00 5 3.59 2
9.00 2 4.61 5 3.49 4
7.46 6 4.46 3 3.44 10
7.09 3 4.37 6 3.39 4
6.72 2 4.27 9 3.34 9
6.38 5 4.09 2 3.31 8
6.00 7 4.01 7 3.25 7 5.72. 6 3.84 100 3.21 5
5.57 6 3.76 34 3.14 2
The Exe naples demonstrate the magadiite, in both natural and synthetic forms, is a suitable source of silica : in the synthesis of ZSM-5 type zeolites. As it is also cheap and readily available magadiite is ry attractive for zeolite synthesis.
Claims (7)
1. A method of preparing a crystalline aluminosilicate zeolite comprising forming a reaction mixture com rising at least one source of aluminium and at least one source of silicon and crystallising the zeolite from the reaction mixture characterised in that the source of silicon comprises, at least in part, a layer silicate.
2. A method as claimed in claim 1 wherein the layer silicate comprises either magadiite or kenyaite in either natural or synthetic form.
3. A method as claimed in claim 1 or 2 in which the reaction mixture comprises at least one source of aluminium, magadiite as the source, at least in part, of silicon and an organic material.
4. A method as claimed in claim 3 in which the organic material is a quaternary ammonium cation.
5. A method as claimed in claim 3 or 4 in which the organic material is a quaternary alkylammonium cation.
6. A method as claimed in any one of claims 3 to 5 in which the organic material is a tetrapropylammonium cation.
7. A method of preparing a crystalline aluminosilicate zeolite substantially as hereinbefore described with reference to any one of examples 1 to 7.
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US4578258A (en) * | 1984-01-04 | 1986-03-25 | Hoechst Aktiengesellschaft | Process for the preparation of crystalline sheet-type alkali metal silicates |
US4581213A (en) * | 1984-01-04 | 1986-04-08 | Hoechst Aktiengesellschaft | Crystalline silicic acid, its salts, and processes for their preparation |
US4582693A (en) * | 1984-11-16 | 1986-04-15 | The Standard Oil Company | Synthesis of silica molecular sieves using synthesis directing organic dyes |
US4626421A (en) * | 1985-06-28 | 1986-12-02 | Chevron Research Company | Preparation of magadiite |
US4676958A (en) * | 1985-03-06 | 1987-06-30 | Chevron Research Company | Preparation of crystalline zeolites using magadiite |
US4689207A (en) * | 1985-03-06 | 1987-08-25 | Chevron Research Company | Process for the preparation of crystalline microporous organosilicates using magadiite as a silica source |
FR2869894A1 (en) * | 2004-05-10 | 2005-11-11 | Inst Francais Du Petrole | METHOD FOR SYNTHESIZING DIRECT SYNTHESIS CRYSTALLIZED METALLOALUMINOSILICATE |
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GB1580918A (en) * | 1976-08-06 | 1980-12-10 | Degussa | Method of producing zeolitic aluminium silicates having a low iron content |
GB1586236A (en) * | 1976-06-29 | 1981-03-18 | Engelhard Min & Chem | Method for producing synthetic sodium aluminosilicate ion-exchange material from calcined kaolin clay |
GB1603084A (en) * | 1977-05-31 | 1981-11-18 | English Clays Lovering Pochin | Zeolites |
-
1983
- 1983-08-08 GB GB08321325A patent/GB2125390B/en not_active Expired
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GB1007853A (en) * | 1961-07-19 | 1965-10-22 | Union Carbide Corp | Process for producing synthetic crystalline zeolites |
GB1035645A (en) * | 1962-07-02 | 1966-07-13 | Grace W R & Co | Preparation of zeolites |
GB1062064A (en) * | 1964-05-13 | 1967-03-15 | British Petroleum Co | Synthetic zeolite production |
GB1132096A (en) * | 1964-10-19 | 1968-10-30 | Union Carbide Corp | Production of molecular sieves |
GB1321460A (en) * | 1969-12-18 | 1973-06-27 | Mobil Oil Corp | Preparation of zeolites |
GB1473607A (en) * | 1974-03-29 | 1977-05-18 | Mobil Oil Corp | Manufacture of zeolites from clay |
GB1586236A (en) * | 1976-06-29 | 1981-03-18 | Engelhard Min & Chem | Method for producing synthetic sodium aluminosilicate ion-exchange material from calcined kaolin clay |
GB1580918A (en) * | 1976-08-06 | 1980-12-10 | Degussa | Method of producing zeolitic aluminium silicates having a low iron content |
GB1571004A (en) * | 1976-10-13 | 1980-07-09 | Mizusawa Industrial Chem | Manufacturing type a zeolite detergent builders |
GB1603084A (en) * | 1977-05-31 | 1981-11-18 | English Clays Lovering Pochin | Zeolites |
GB2030974A (en) * | 1978-09-08 | 1980-04-16 | Norton Co | Mordenite Synthesis |
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4578258A (en) * | 1984-01-04 | 1986-03-25 | Hoechst Aktiengesellschaft | Process for the preparation of crystalline sheet-type alkali metal silicates |
US4581213A (en) * | 1984-01-04 | 1986-04-08 | Hoechst Aktiengesellschaft | Crystalline silicic acid, its salts, and processes for their preparation |
US4582693A (en) * | 1984-11-16 | 1986-04-15 | The Standard Oil Company | Synthesis of silica molecular sieves using synthesis directing organic dyes |
US4676958A (en) * | 1985-03-06 | 1987-06-30 | Chevron Research Company | Preparation of crystalline zeolites using magadiite |
US4689207A (en) * | 1985-03-06 | 1987-08-25 | Chevron Research Company | Process for the preparation of crystalline microporous organosilicates using magadiite as a silica source |
US4626421A (en) * | 1985-06-28 | 1986-12-02 | Chevron Research Company | Preparation of magadiite |
FR2869894A1 (en) * | 2004-05-10 | 2005-11-11 | Inst Francais Du Petrole | METHOD FOR SYNTHESIZING DIRECT SYNTHESIS CRYSTALLIZED METALLOALUMINOSILICATE |
EP1595846A2 (en) * | 2004-05-10 | 2005-11-16 | Institut Français du Pétrole | Method for synthesizing crystallized metalloaluminosilicate by direct synthesis |
EP1595846A3 (en) * | 2004-05-10 | 2007-05-23 | Institut Français du Pétrole | Method for synthesizing crystallized metalloaluminosilicate by direct synthesis |
Also Published As
Publication number | Publication date |
---|---|
GB8321325D0 (en) | 1983-09-07 |
GB2125390B (en) | 1985-12-24 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
PCNP | Patent ceased through non-payment of renewal fee |
Effective date: 19920808 |