IP Library Granted Patent US 7,642,365
Granted Patent B2
US 7,642,365 · App. 11/890,183 · Granted Jan 5, 2010

Multiphase reactor design incorporating filtration system for fixed—bed catalyst

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Quick Facts
Patent No.
US 7,642,365
App. No.
11/890,183
Granted
Jan 5, 2010
Kind
B2
Abstract

A unique reactor configuration especially suitable for interphase mass transfer and mixing of multiple phases, i.e. gas(es), liquid(s), and solid(s) where reaction is catalyzed by a solid catalyst comprises a draught tube reactor wherein the solid catalyst particles are maintained in an annular space between the draught tube of the reactor and an annulus-defining wall by means of filter elements positioned downstream and optionally also upstream from the catalyst bed.

Claims (22)

1. In a process for the epoxidation of an olefin in the presence of a solid catalyst in a liquid reaction medium, the improvement comprising

epoxidizing said olefin in a reactor having a central draft tube located within said reactor, at least one impeller located within said draft tube, an annular space between the draft tube and a wall of the reactor, and a fluid flow path in only one direction within the draft tube and only countercurrent flow, relative to the direction of fluid flow within the draft tube, through the annular space, said reactor having

a) a catalyst bed for the solid catalyst located within said annular space;

b) a filter element in said annular space positioned downstream from said catalyst bed relative to the direction of fluid flow through said annular space, said filter element having pores therein to allow fluid flow through said filter element, said pores of sufficiently small size so to substantially prevent catalyst particles from leaving said catalyst bed;

c) a second filter element having pores therein to allow fluid flow through said second filter element in said annular space upstream from said catalyst bed relative to the direction of fluid flow through said annular space;

said reactor having at least one inlet for an inlet feed stream and at least one product outlet for a product stream,

wherein the catalyst bed is contained with a catalyst basket located within said reactor, said catalyst basket comprising:

i) a central tube and a larger annulus-defining tube; and

ii) a top ring and a bottom ring, each of said top and bottom rings fixed to both said central tube and said annulus-defining tube, the space between said central tube and said annulus defining tube defining an annular space suitable for receiving a charge of said solid catalyst;

wherein said filter element is positioned above said top ring or within said top ring such that fluid entering said annular space passes through said first filter element,

said second filter element is positioned below said bottom ring or within said bottom ring such that fluid leaving said annular space passes through said second filter element, and

said central tube surrounding said draft tube or comprising said draft tube,

and separating olefin oxide from the product stream thereof.

2. The process of claim 1 , wherein said liquid reaction medium comprises an oxygen-containing solvent.

3. The process of claim 1 , wherein said solid catalyst comprises a titanium silicalite catalyst.

4. The process of claim 3 , wherein said inlet feed stream comprises hydrogen and oxygen and said solid catalyst comprises titanium silicalite treated to contain a noble metal.

5. The process of claim 3 , wherein said solid catalyst is an agglomerate of the titanium silicalite bound together with a binder.

6. The process of claim 1 , wherein said draft tube contains one or more baffles oriented vertically within said draft tube, and proximate one or more of the impellers.

7. The process of claim 1 , wherein one or more of the inlets terminates proximate to an upstream end of said draft tube, relative to the direction of fluid flow within said draft tube, or terminates within said draft tube.

8. The process of claim 1 , wherein said product outlet is located downstream from said annular space relative to the direction of fluid flow through said annular space.

9. The process of claim 1 , wherein the reactor has a filter support plate positioned intermediate said top ring and said first filter element.

10. The process of claim 1 , wherein the reactor has a filter support plate positioned intermediate said bottom ring and said second filter element.

Assignments (17)
RELEASE OF SECURITY INTEREST Recorded Jan 23, 2014
From: DEUTSCHE BANK TRUST COMPANY AMERICAS
To: LYONDELL CHEMICAL TECHNOLOGY, L.P.
Reel/Frame 032123/0799 →
RELEASE OF SECURITY INTEREST Recorded Jan 23, 2014
From: BANK OF AMERICA, N.A.
To: LYONDELL CHEMICAL TECHNOLOGY, L.P.
Reel/Frame 032138/0134 →
RELEASE OF SECURITY INTEREST Recorded Jan 23, 2014
From: CITIBANK, N.A.
To: LYONDELL CHEMICAL TECHNOLOGY, L.P.
Reel/Frame 032125/0296 →
RELEASE OF SECURITY INTEREST Recorded Jan 23, 2014
From: WELLS FARGO BANK, NATIONAL ASSOCIATION
To: LYONDELL CHEMICAL TECHNOLOGY, L.P.
Reel/Frame 032137/0156 →
APPOINTMENT OF SUCCESSOR ADMINISTRATIVE AGENT Recorded Jan 23, 2014
From: UBS AG, STAMFORD BRANCH
To: BANK OF AMERICA, N.A.
Reel/Frame 032137/0639 →
SECURITY AGREEMENT Recorded May 19, 2010
From: LYONDELL CHEMICAL TECHNOLOGY, L.P.
To: WELLS FARGO BANK, NATIONAL ASSOCIATION, AS COLLATERAL AGENT
Reel/Frame 024402/0681 →
SECURITY AGREEMENT Recorded May 18, 2010
From: LYONDELL CHEMICAL TECHNOLOGY, L.P.
To: CITIBANK, N.A., AS ADMINISTRATIVE AGENT
Reel/Frame 024397/0818 →
SECURITY AGREEMENT Recorded May 7, 2010
From: LYONDELL CHEMICAL TECHNOLOGY, L.P.
To: UBS AG, STAMFORD BRANCH, AS COLLATERAL AGENT
Reel/Frame 024342/0801 →
SECURITY AGREEMENT Recorded May 6, 2010
From: LYONDELL CHEMICAL TECHNOLOGY, L.P.
To: DEUTSCHE BANK TRUST COMPANY AMERICAS, AS COLLATERAL AGENT
Reel/Frame 024342/0421 →
RELEASE OF SECURITY INTEREST Recorded May 5, 2010
From: CITIBANK, N.A., AS COLLATERAL AGENT
To: LYONDELL CHEMICAL TECHNOLOGY, L.P.; EQUISTAR CHEMICALS, LP
Reel/Frame 024337/0856 →
RELEASE OF SECURITY INTEREST Recorded May 5, 2010
From: CITIBANK, N.A., AS COLLATERAL AGENT
To: LYONDELL CHEMICAL TECHNOLOGY, LP
Reel/Frame 024337/0020 →
RELEASE OF SECURITY INTEREST Recorded May 5, 2010
From: UBS AG, STAMFORD BRANCH, AS COLLATERAL AGENT
To: LYONDELL CHEMICAL TECHNOLOGY, LP
Reel/Frame 024337/0285 →
RELEASE OF SECURITY INTEREST Recorded May 5, 2010
From: CITIBANK, N.A., AS COLLATERAL AGENT
To: LYONDELL CHEMICAL TECHNOLOGY, L.P.; EQUISTAR CHEMICALS, LP
Reel/Frame 024337/0705 →
SECURITY AGREEMENT Recorded Oct 30, 2009
From: LYONDELL CHEMICAL TECHNOLOGY, L.P.
To: UBS AG, STAMFORD BRANCH, AS COLLATERAL AGENT
Reel/Frame 023449/0138 →
SECURITY AGREEMENT Recorded Apr 9, 2009
From: LYONDELL CHEMICAL TECHNOLOGY, L.P.
To: CITIBANK, N.A., AS ADMINISTRATIVE AGENT AND COLLATERAL AGENT
Reel/Frame 022708/0830 →
SECURITY AGREEMENT Recorded Aug 4, 2008
From: BASELL POLYOLEFINE GMBH; ARCO CHEMICAL TECHNOLOGY L.P.; ARCO CHEMICAL TECHNOLOGY, INC.; ATLANTIC RICHFIELD COMPANY; BASELL NORTH AMERICA, INC.; BASELL POLYOLEFIN GMBH; LYONDELL CHEMICAL COMPANY; EQUISTAR CHEMICALS, L.P.
To: CITIBANK, N.A., AS COLLATERAL AGENT
Reel/Frame 021354/0708 →
GRANT OF SECURITY INTEREST IN UNITED STATES PATENTS AND PATENT APPLICATIONS Recorded Mar 26, 2008
From: BASELL POLYOLEFINE GMBH; ARCO CHEMICAL TECHNOLOGY L.P.; ARCO CHEMICAL TECHNOLOGY, INC.; ATLANTIC RICHFIELD COMPANY; BASELL NORTH AMERICA, INC.; EQUISTAR CHEMICALS. LP.; LYONDELL CHEMICAL COMPANY; LYONDELL CHEMICAL TECHNOLOGY, L.P.; LYONDELL PETROCHEMICAL COMPANY; NATIONAL DISTILLERS AND CHEMICAL CORPORATION; OCCIDENTAL CHEMICAL CORPORATION; OLIN CORPORATION; QUANTUM CHEMICAL CORPORATION; BASELL POLYOLEFIN GMBH
To: CITIBANK, N.A., AS COLLATERAL AGENT
Reel/Frame 020704/0562 →