GB1354981A – Thermally stable catalytically active zeolite
– Google Patents
GB1354981A – Thermally stable catalytically active zeolite
– Google Patents
Thermally stable catalytically active zeolite
Info
Publication number
GB1354981A
GB1354981A
GB1696971A
GB1696971A
GB1354981A
GB 1354981 A
GB1354981 A
GB 1354981A
GB 1696971 A
GB1696971 A
GB 1696971A
GB 1696971 A
GB1696971 A
GB 1696971A
GB 1354981 A
GB1354981 A
GB 1354981A
Authority
GB
United Kingdom
Prior art keywords
faujasite
ion
catalytically active
thermally stable
exchange
Prior art date
1970-08-26
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
Application number
GB1696971A
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
WR Grace and Co Conn
WR Grace and Co
Original Assignee
WR Grace and Co Conn
WR Grace and Co
Priority date (The priority date 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 date listed.)
1970-08-26
Filing date
1971-05-25
Publication date
1974-06-05
1971-05-25
Application filed by WR Grace and Co Conn, WR Grace and Co
filed
Critical
WR Grace and Co Conn
1974-06-05
Publication of GB1354981A
publication
Critical
patent/GB1354981A/en
Status
Expired
legal-status
Critical
Current
Links
Espacenet
Global Dossier
Discuss
Classifications
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
C10G11/00—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
C10G11/02—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils characterised by the catalyst used
C10G11/04—Oxides
C10G11/05—Crystalline alumino-silicates, e.g. molecular sieves
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
B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
B01J20/10—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising silica or silicate
B01J20/16—Alumino-silicates
B01J20/18—Synthetic zeolitic molecular sieves
B01J20/186—Chemical treatments in view of modifying the properties of the sieve, e.g. increasing the stability or the activity, also decreasing the activity
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
B01J29/00—Catalysts comprising molecular sieves
B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
B01J29/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
B01J29/08—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the faujasite type, e.g. type X or Y
Abstract
1354981 Rare earth faujasite W R GRACE & CO 25 May 1971 [26 Aug 1970] 16969/71 Heading C1A [Also in Divisions B1 and C5] R. E. faujasite is prepared by: (a) ion-exchanging an A.M. faujasite having a SiO 2 : Al 2 O 3 molar ratio of 3 : 1-6 : 1 with an aq. soln. of R.E. metal ions at a pH of 3À0- 3-5 to reduce the A.M. oxide to <6% by wt., (b) calcining the exchanged faujasite at 800- 1400‹ F. for a period of 1-3 hrs. and then, (c) ion-exchanging the calcined faujasite with a soln. of NH 4
Download PDF in English