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US2417348A - Process of lining catalyst chambers - Google Patents

Process of lining catalyst chambers Download PDF

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Publication number
US2417348A
US2417348A US481031A US48103143A US2417348A US 2417348 A US2417348 A US 2417348A US 481031 A US481031 A US 481031A US 48103143 A US48103143 A US 48103143A US 2417348 A US2417348 A US 2417348A
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United States
Prior art keywords
chamber
liner
liners
catalyst
sectional
Prior art date
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Expired - Lifetime
Application number
US481031A
Inventor
Charles E Carter
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Phillips Petroleum Co
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Phillips Petroleum Co
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Publication date
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Priority to US481031A priority Critical patent/US2417348A/en
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Publication of US2417348A publication Critical patent/US2417348A/en
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/02Apparatus characterised by being constructed of material selected for its chemically-resistant properties
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/0053Details of the reactor
    • B01J19/0073Sealings
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/008Details of the reactor or of the particulate material; Processes to increase or to retard the rate of reaction
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008Controlling the process
    • B01J2208/00017Controlling the temperature
    • B01J2208/00477Controlling the temperature by thermal insulation means
    • B01J2208/00495Controlling the temperature by thermal insulation means using insulating materials or refractories
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00049Controlling or regulating processes
    • B01J2219/00051Controlling the temperature
    • B01J2219/0015Controlling the temperature by thermal insulation means
    • B01J2219/00155Controlling the temperature by thermal insulation means using insulating materials or refractories
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/02Apparatus characterised by their chemically-resistant properties
    • B01J2219/0204Apparatus characterised by their chemically-resistant properties comprising coatings on the surfaces in direct contact with the reactive components
    • B01J2219/0245Apparatus characterised by their chemically-resistant properties comprising coatings on the surfaces in direct contact with the reactive components of synthetic organic material

Definitions

  • the catalyst mass and the chamber may be raised to temperatures within the range of about 1000o to 1500 F. These elevated temperatures are attained in the presence of free oxygen-containing fluids, such as air; and by virtue thereof, ordinary metals, when directly subjected to such temperatures, deteriorate rather quickly. Moreover, high temperatures are required during the conversion period, and since the conversion is often endothermic, it is desirable to minimize heat losses in order to maintain an ecient rate of conversion. For these reasons it has become desirable and con.- venient to insulate the interior of the usual metal catalyst chamber with a liner of insulating material that is preferably of the refractory type. Such a liner protects the metal chamber from, the detrimental effects of high temperatures, and in some cases enables the use of carbon steel instead of more expensive special alloy metals.
  • Suitable heat resistant materials are preferably applied to the interior Walls of the chamber by casting the same therein.
  • Vapor-tight liners are extremely dliiicult to form because of the tendency of the insulating materials, such as refractory cements, to shrink on setting after being cast in the form of a plastic mass. This is especially true vin the case of relatively large chambers, and particularly those of extended length.
  • insulating materials such as refractory cements
  • the liners tend to crack, due to shrinkage on becoming set.
  • improved liners may be fabricated when they are cast in a plurality of sections on the inner surface of a side Wall of a catalyst chamber to form a laminated type structure. For one thing, v the stresses set up in individual sections are isolated and do not4 alect any adjoining' sections.
  • Another object of this invention is to provide a sectional inner liner of cast heat-insulating material on the inner surface of the tubular wall of a catalyst chamber, which liner does not tend to become checked or cracked upon setting and in the course of normal use.
  • I have generally denoted a catalyst chamber by 'reference numeral I 0, which chamber includes a substantially vertical' side wall Il, a topwa1l ⁇ l2 having an inlet I3 that communiel tes'with the interior of the chamber, and a bo tom wall I4 having an outlet I5 through wlfich the conversion prod-
  • the chamber is preferably of a conventional type having a removal top mits ready access to the interior for purposes of repair and removal vor insertion of linervor ⁇ operation; an external sheath of insulating mabetween the abutting surfacesV of the wall or cover which percatalytic materials.
  • Side ⁇ wall .II- consists of a I substantially cylindrical 'and vertical tubular.
  • inner ⁇ liner I8 consists of a plurality of annular sections i9, 20, 2i. and' 22 that are disposed one above the other in an abutting relation, as illustrated. The upper end surface of.
  • sectional liners I9, 20, and 2i- are each provi ed withat least one annular groove 23, prefera ly V-shaped, which is adapted to receive an annular tongue or projection 24 in the lower end surface of the adjacent and abutting sectional liner immediately thereabove.
  • a coating of sealing material, such as a suitable grease, is interposed sectional liners during fabrication.
  • lower sectional liner i9 is first cast in the lower portion of metal shell I6 and is allowed to set or substantially solidify.
  • Corresponding groove 23 is then formed in the upper surface of lower section [9,01* if desired, said groove may be 'formed while the material of the liner is still in a plastic state.
  • sectional liner I9 becomes substantially set.
  • the4 upper end surface thereof, including corresponding groove 23 is coated with a sealing material of the character indicated above.
  • Sectional liner 20 is then cast directly upon sectional liner i9, annular projection 24 extending into groove 23 in sectional liner I9. The procedure. outlined herein is then repeated with respect yto the remaining sectional liners.

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Description

March 1l, 1947. c. E. CARTER PROCESS OFLINNG CATALYST'CHAMBER Filed arch 29. 1943 INVENTOR CHARLES E. CARTER QM; f7. ATTORNEYS Patented Mar. 1l, 1947 PROCESS OF LINING CATAL-YST CHADIBERS Charles E. Carter, Kansas City, Mo., assignor to Phillips Petroleum Company, a corporation of Delaware Application March 29, 1943, Serial No. 481,031
1 Claim. v ll This invention relates to improvements in the construction of catalyst chambersl of the class employed in carrying out ln'drocarbon conversions in the presence of solid catalyst material,
the carbonaceous deposits. As a result of the exoy thermic heat of combustion developed in the course of catalyst reactivation, the catalyst mass and the chamber may be raised to temperatures within the range of about 1000o to 1500 F. These elevated temperatures are attained in the presence of free oxygen-containing fluids, such as air; and by virtue thereof, ordinary metals, when directly subjected to such temperatures, deteriorate rather quickly. Moreover, high temperatures are required during the conversion period, and since the conversion is often endothermic, it is desirable to minimize heat losses in order to maintain an ecient rate of conversion. For these reasons it has become desirable and con.- venient to insulate the interior of the usual metal catalyst chamber with a liner of insulating material that is preferably of the refractory type. Such a liner protects the metal chamber from, the detrimental effects of high temperatures, and in some cases enables the use of carbon steel instead of more expensive special alloy metals.
Furthermore, the use of such a liner greatly reduces heat losses that would otherwise occur in the conversion process. Suitable heat resistant materials are preferably applied to the interior Walls of the chamber by casting the same therein.
In the casting of liners of the character indicated, care must be taken to make the same substantially vapor-tight in order that the hot gases and/or vapors within the chamber may not pass through cracks and other continuous passages through the liner and reach the metal shell. When this occurs liners may be detached from the shell and the hot fluids may channel between the detached liner and the inner surface of the shell, thereby 'oy-passing the catalyst bed. Such an eventuality results in unsatisfactory operation,
heat losses through the chamber, and incomplete 'ucts are discharged from the chamber.
conversion of the process material. Vapor-tight liners are extremely dliiicult to form because of the tendency of the insulating materials, such as refractory cements, to shrink on setting after being cast in the form of a plastic mass. This is especially true vin the case of relatively large chambers, and particularly those of extended length. Experience has proven that when present day methodsy of insulating the interior of such liners are employed, the liners tend to crack, due to shrinkage on becoming set. I have discovered that improved liners may be fabricated when they are cast in a plurality of sections on the inner surface of a side Wall of a catalyst chamber to form a laminated type structure. For one thing, v the stresses set up in individual sections are isolated and do not4 alect any adjoining' sections. As
will be readily apparent to those skilled in the,
art upona complete vexamination of this invention as disclosed herein, the practice thereof affords a number of desirable advantages over the Well-known catalyst chambers. The liners of my invention eliminate the'possibility of objectionable cracks extending therethrough along the entire length of the chamber shell. Additionally,
there is less likelihood of any Acracks being formed Whenthe insulating material sets and solidies.
It is the primary object of this invention to provide a catalyst chamber ,having an inner liner of insulating material -of improved construction and adapted to perform its intended functions in a wholly satisfactory manner.
Another object of this invention is to provide a sectional inner liner of cast heat-insulating material on the inner surface of the tubular wall of a catalyst chamber, which liner does not tend to become checked or cracked upon setting and in the course of normal use. l
These, as well as other objects yand advantages,
will be readily apparent from an examination of the following detailed description taken in conjunction with the annexed drawing, wherein Athere isillustrated a preferred embodiment of the invention in elevation and partly in cross section particularly showing a preferred V-shaped groove and abutting tongue of insulating material.
Referring to the drawing, I have generally denoted a catalyst chamber by 'reference numeral I 0, which chamber includes a substantially vertical' side wall Il, a topwa1l`l2 having an inlet I3 that communiel tes'with the interior of the chamber, and a bo tom wall I4 having an outlet I5 through wlfich the conversion prod- The chamber is preferably of a conventional type having a removal top mits ready access to the interior for purposes of repair and removal vor insertion of linervor` operation; an external sheath of insulating mabetween the abutting surfacesV of the wall or cover which percatalytic materials. Side `wall .II- consists of a I substantially cylindrical 'and vertical tubular. wall it, that is fabricated from sheet or plate lmetal of requisite thickness and composition to withstand the temperature and pressure condltions to which it is subjected during normal terial` il preferably of the asbestos type; and an inner liner I8 of cast insulating material, preferably of the refractory type. inner `liner I8 consists of a plurality of annular sections i9, 20, 2i. and' 22 that are disposed one above the other in an abutting relation, as illustrated. The upper end surface of. sectional liners I9, 20, and 2i-is each provi ed withat least one annular groove 23, prefera ly V-shaped, which is adapted to receive an annular tongue or projection 24 in the lower end surface of the adjacent and abutting sectional liner immediately thereabove. A coating of sealing material, such as a suitable grease, is interposed sectional liners during fabrication.
In the course of the manufacture of the catalyst chamber, lower sectional liner i9 is first cast in the lower portion of metal shell I6 and is allowed to set or substantially solidify. Corresponding groove 23 is then formed in the upper surface of lower section [9,01* if desired, said groove may be 'formed while the material of the liner is still in a plastic state. As soon as sectional liner I9 becomes substantially set. the4 upper end surface thereof, including corresponding groove 23, is coated with a sealing material of the character indicated above. Sectional liner 20 is then cast directly upon sectional liner i9, annular projection 24 extending into groove 23 in sectional liner I9. The procedure. outlined herein is then repeated with respect yto the remaining sectional liners. It will be noted that by virtue` of the ring and groove arrangement at the juncture of the sectional liners an effective seal is obtained. Furthermore, should the iiuid material admitted into the chamber tend to pass through this joint, it would be hindered by virtue of the extended path it would have to follow, as compared to the thickness of the liner. If desired, more than one groove and annular projection arrangement may be provided to thereby further increase said path. While I y claim.
have disclosed the use of a suitable grease as the coating material between the sectional liners,
Acomprehended by persons skilled in the art. It
is to be clearly understood,'however, thatvarious changes in the method herein set forth, may
be resorted to without departing from the spirit of the invention as .dened by the4 appended r claim: l e In the insulation of a chamberfor the catalytic conversion of hydrocarbons, the process of installing refractory material for the protection of the walls of said chamber, which comprises y casting a rst section of hard-setting, heat-insulating, plastic material in the inner surface of the lower portion of said chamber wall, forming at least one annular Vshaped groove substantially concentric with said chamber wall in the upper edge of said cast section, allowing said rst section to set and assume substantially its maximum contraction, casting a relatively narrow section of said insulating material above said first section with a tongue tting into said groove to form a vapor-tight unannexed joint between said sections and allowing a similar pe` riod for setting and contraction, and successively repeating the operation of casting relatively' narrow sections of insulation with similar setting and contracting 'periods of time between each successive layer to completely line the inner surface of said chamber with vapor-tight sections of insulation.
CHARLES E.. CARTER.
REFERENCES cl'rEn The following references are o f record in the le of this patent:
UNITED STATES PaTEN'rs
US481031A 1943-03-29 1943-03-29 Process of lining catalyst chambers Expired - Lifetime US2417348A (en)

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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2535944A (en) * 1946-09-19 1950-12-26 Phillips Petroleum Co Catalytic apparatus
US2584080A (en) * 1947-04-24 1952-01-29 American Cyanamid Co Apparatus for reacting ammoniacal gases
US2903876A (en) * 1955-01-24 1959-09-15 Phillips Petroleum Co Furnace or reactor
US3308589A (en) * 1962-12-22 1967-03-14 Yawata Iron & Steel Co Layered curvilinear wall
US3311690A (en) * 1963-03-13 1967-03-28 Continuous Molding Corp Injection molding method for encapsulating metal objects

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1021082A (en) * 1911-09-27 1912-03-26 William Wright Expansion-joint.
US1103470A (en) * 1913-07-14 1914-07-14 George F Bason Tank.
US1860590A (en) * 1929-09-07 1932-05-31 Fred A Noetzli Method of constructing dams
US2106828A (en) * 1935-03-11 1938-02-01 Eugene L Chappell Method of making a lined container
US2339892A (en) * 1941-10-20 1944-01-25 William E Urschel Machine for building walls

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1021082A (en) * 1911-09-27 1912-03-26 William Wright Expansion-joint.
US1103470A (en) * 1913-07-14 1914-07-14 George F Bason Tank.
US1860590A (en) * 1929-09-07 1932-05-31 Fred A Noetzli Method of constructing dams
US2106828A (en) * 1935-03-11 1938-02-01 Eugene L Chappell Method of making a lined container
US2339892A (en) * 1941-10-20 1944-01-25 William E Urschel Machine for building walls

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2535944A (en) * 1946-09-19 1950-12-26 Phillips Petroleum Co Catalytic apparatus
US2584080A (en) * 1947-04-24 1952-01-29 American Cyanamid Co Apparatus for reacting ammoniacal gases
US2903876A (en) * 1955-01-24 1959-09-15 Phillips Petroleum Co Furnace or reactor
US3308589A (en) * 1962-12-22 1967-03-14 Yawata Iron & Steel Co Layered curvilinear wall
US3311690A (en) * 1963-03-13 1967-03-28 Continuous Molding Corp Injection molding method for encapsulating metal objects

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