Radial flow catalytic reactor including heat exchange apparatus within the bed

• US 4,714,592 A
• Filed: 01/09/1985
• Issued: 12/22/1987
• Est. Priority Date: 01/18/1984
• Status: Expired due to Fees

• Current Assignee: TOYO Engineering Corporation
• Original Assignee: TOYO Engineering Corporation
• Inventors: Shimagaki, Makoto, Nakajima, Yoichi, Zanma, Jun, Shyoji, Kazuo, Nishimura, Yoshinori
• Primary Examiner(s): Lacey, David L.
• Application Number:
  US06/690,028
• Time in Patent Office: 1,077 Days
• Field of Search: 422/148, 422/191, 422/192, 422/193, 422/195, 422/200, 422/201, 422/202, 422/218, 165/145, 165/163, 165/157, 122/32, 518/706, 423/359-361
• US Class Current: 422/637
• CPC Class Codes: B01J 2208/00132 Tubes
• CPC Class Codes: B01J 8/0285 Heating or cooling the reactor for tubular reactors in furnaces B01J8/062
• CPC Class Codes: B01J 8/0403 the fluid flow within the beds being predominantly horizontal

Abstract

An improved reactor is disclosed wherein a high temperature product gas discharged from a catalyst bed within the reactor is cooled in a central heat exchanger installed within the reactor by heat exchange with a low temperature feed gas comprising gaseous raw materials for the reaction, and the product gas is thereafter flowed along the inner surface of an outer pressure vessel in order to maintain the outer pressure vessel at a low temperature. Inlet and outlet pipes for a coolant which coolant is circulated through a coolant passage structure which penetrates the catalyst bed in order to absorb the heat of reaction, both penetrate the top cover of the outer pressure vessel so that the coolant passage structure can be readily removed for maintenance and inspection, and the overall design of the reactor is simplified.

Claims

1. In a reactor including an outer pressure vessel having an inlet passage for feeding gaseous feed materials into said pressure vessel and an outlet passage for discharging a product gas therefrom, a bed of a granular catalyst and means for flowing a reactant gas comprising the gaseous feed materials through said granular catalyst so that it reacts to form a product gas, means for cooling the product gas and preheating the gaseous feed materials, and means for cooling the reactant gas as the reactant gas passes through said catalyst bed, the improvement which comprises:

said outer pressure vessel is upright and cylindrical, and comprises a bottom cover and a removable top cover;

said cooling and preheating means comprises a heat exchanger centrally mounted within said outer pressure vessel coaxially therewith, said heat exchanger comprising a substantially cylindrical outer shell, upper and lower partition plates subdividing the interior of said shell in the lengthwise direction thereof, a plurality of heat exchanger tubes extending from said upper partition plate to said lower partition plate, said heat exchanger tubes opening above said upper partition plate and opening below said lower partition plate, said partition plates being positioned so as to define a shell-side heat exchange compartment therebetween, an upper chamber above said upper partition plate and a lower chamber below said lower partition plate, said shell of said heat exchanger having openings at opposite end portions thereof so that a gas can enter said compartment near one end of said compartment and be discharged from the opening at the other end of said compartment, said inlet passage for the gaseous feed materials being in communication with said shell-side heat exchage compartment of said heat exchanger so that the gaseous feed materials undergo heat exchange and are thereby preheated before being fed to said catalyst bed;

said catalyst bed comprises spaced-apart inner and outer cylindrical gas-permeable catalyst retainers being positioned and arranged so as to define an intercylinder space therebetween coaxial with said outer pressure vessel and said heat exchanger, said inner catalyst retainer being of smaller diameter than said outer catalyst retainer, and a bottom wall extending beneath said catalyst retainers and fixedly connecting said catalyst retainers to each other, said catalyst retainers and said bottom wall being spaced apart from the inner periphery of said outer pressure vessel, said granular catalyst being packed in the intercylinder space between said inner and outer catalyst retainers above said bottom wall;

said cooling means comprises a cooling structure having a coolant inlet passage and a coolant outlet passage which both extend through said top cover of said outer pressure vessel, and a multiplicity of vertical cooling tubes which extend through said catalyst bed, said granular catalyst being packed around said cooling tubes, each of said cooling tubes being in communication with said coolant inlet passage and said coolant outlet passage so that a liquid coolant may be circulated through said cooling structure to absorb reaction heat generated in said catalyst bed;

a cylindrical, gas-impermeable, outer, partition wall coaxial with said outer pressure vessel and located between said outer pressure vessel and said outer gas-permeable catalyst retainer and spaced therefrom and positioned so as to define a first outer gas flow passageway between said outer pressure vessel and said cylindrical outer partition wall and a second inner gas flow passageway between said cylindrical outer partition wall and said outer catalyst retainer, whereby the product gas from said catalyst bed is discharged through said outer catalyst retainer into said second inner gas flow passageway, flows through said second inner flow passageway and thence into the tubes of said heat exchanger, undergoes heat exchange with the gaseous feed materials, in said heat exchanger, thereby cooling the product gas, and then is fed through said first outer gas flow passageway to said product gas outlet formed on said outer pressure vessel.

16. A reactor as claimed in claim 1 or claim 15, further comprising a plurality of upright, radially extending partition walls which span said inner and outer catalyst retainers to thereby define a plurality of separate catalyst beds which are sectorial in horizontal cross section, a plurality of radially extending partition walls within said second inner gas flow passage which subdivide said second inner gas flow passage into a plurality of second inner gas flow passage sections, and a plurality of radially extending partition walls within an internal gas flow passage defined between said outer shell of said heat exchanger and said inner catalyst retainer which partition walls subdivide said internal gas flow passage into a plurality of internal gas flow passage sections, all of said partition walls being positioned so that the reactant gas is first fed through said heat exchanger and preheated therein, and then fed alternately radially inwardly and radially outwardly through said catalyst beds in series by said gas flow passage sections, the reactant gas passing alternately through one of said second inner gas flow passage sections, then radially through one of said catalyst beds, then through one of said internal gas flow passage sections to the next catalyst of said beds in series.

2. A reactor for effecting a catalytic reaction wherein pressurized gaseous feed materials containing hydrogen contact a granular catalyst at an elevated temperature to form a high temperature reaction product gas, said reactor comprising:

a cylindrical, vertical, outer, pressure vessel having a top cover, a bottom cover, an inlet for the gaseous feed materials and an outlet for the reaction product gas;

a shell-and-tube heat exchanger centrally mounted within said outer pressure vessel and coaxial therewith, said heat exchager comprising a vertically mounted cylindrical outer shell, upper and lower partition plates inside said shell defining the upper and lower ends of a shell-side heat exchange compartment therein and also defining upper and lower chambers within said shell which upper and lower chambers do not communicate with said compartment and a plurality of heat exchange tubes which penetrate said partition plates and extend into and through said compartment but do not communicate therewith, said heat exchanger having a heat transfer area sufficient to preheat low temperature gaseous feed materials and to cool the high temperature reaction product gas to a temperature below 300°

C., by flowing the gaseous feed materials and the reaction product gas in indirect heat exchanging relationship in said heat exchanger;

inner and outer, coaxial, cylindrical, gas-permeable, catalyst retainers, said catalyst retainers being mounted within said pressure vessel coaxially therewith and located between said shell of said heat exchanger and said pressure vessel, said inner and outer catalyst retainers positioned so as to define an annular intercylinder space;

a bottom wall extending beneath said catalyst retainers and fixedly connecting said catalyst retainers to each other;

granular catalyst bed means packed in said intercylinder space between said catalyst retainers above said bottom wall;

first feed gas passage means for conducting the gaseous feed materials to said shell-side heat exchange compartment, and second feed gas passage means for introducing preheated gasous feed materials discharged from said shell-side heat exchange compartment of said heat exchanger into said catalyst bed means and flowing the preheated gaseous feed materials radially through said catalyst bed means;

first reaction product gas passage means for conducting the high temperature reaction product gas discharged from said catalyst bed means to said heat exchange tubes of said heat exchanger for indirect heat exchange interaction with the gaseous feed materials whereby to cool the reaction product gas and to heat the gaseous feed materials;

second reaction product gas passage means for receiving the cooled reaction product gas discharged from said heat exchange tubes of said heat exchanger;

a cooling passage structure for indirectly cooling the contents of said catalyst bed means by passing a liquid coolant therethrough, the liquid coolant having a boiling point temperature which permits the liquid coolant to boil when subjected to an elevated temperature and pressure, said coolant passage structure comprising coolant inlet passage means and coolant outlet passage means both extending through said top cover of said outer pressure vessel, at least one coolant distributing header for receiving coolant from said coolant inlet passage means and at least one coolant collecting header for supplying coolant to said coolant outlet passage means and a multiplicity of vertical cooling tubes which extend vertically within said catalyst bed means, said cooling tubes being arranged in at least one arcuate formation concentric with the vertical axis of said outer pressure vessel, the lower end of each of said cooling tubes being connected with said coolant inlet passage means by said at least one coolant distributing header and the upper end of each of said cooling tubes being connected with said coolant outlet passage means by said at least one coolant collecting header, so that the coolant may be circulated through said cooling passage structure, said coolant inlet passage means supplying the liquid coolant to the lower ends of said cooling tubes by said at least one distributing header and said coolant outlet passage means discharging vapor of the coolant or a liquid-vapor mixture of the coolant collected by said at least one collecting header from the upper ends of said cooling tubes; and

a cylindrical, gas-impermeable, outer, partition wall having a heat insulating layer thereon, said gas-impermeable outer partition wall being mounted coaxially within said pressure vessel and being located between and spaced from said pressure vessel and said outer, gas-permeable, catalyst retainer, said cylindrical outer partition wall being positioned and arranged so as to define a first elongated passageway between said pressure vessel and said cylindrical outer partition wall and defining a second elongated passageway between said cylindrical outer partition wall and said outer catalyst retainer, which first and second passageways are not in direct communication with each other, one end of said first passageway being in direct communication with said outlet for the product gas, the other end of said first passageway being connected to said second reaction product gas passage means so that the cooled reaction product gas discharged from said heat exchanger flows into and through said first passageway, said second passageway being connected with said first reaction product gas passage means for directing the high temperature reaction product gas discharged from said catalyst bed means into said heat exchange tubes of said heat exchanger.

3. A reactor as claimed in claim 2, wherein said first feed gas passage means for the gaseous feed materials comprises an inlet pipe which successively penetrates said top cover of said outer pressure vessel, said shell of said heat exchanger, and said top partition plate of said heat exchanger, said inlet pipe opening into said shell-side heat exchange compartment of said heat exchanger so that the gaseous feed materials flow downwardly therein, said shell having lateral openings at a lower and portion thereof so that the gaseous feed materials flow radially outwardly out of said compartment through said openings, then pass through said second feed gas passage means between said outer shell of said heat exchanger and said inner catalyst retainer, then flow radially outwardly through said inner catalyst retainer into said catalyst bed, then flow out of said catalyst bed through said outer catalyst retainer into said second passageway and thence into said first reaction product gas passage means, and the thus-formed product gas then is fed to said lower chamber within said heat exchanger, then passes upwardly through said heat exchanger tubes, then passes into said upper chamber of said heat exchanger, then passes radially outwardly into said second reaction product gas passage means and thence into said first passageway, the reaction product gas then flows to said product gas outlet and is discharged therethrough.

5. A reactor as claimed in claim 2 or claim 4, wherein the intercylinder space between said catalyst retainers is divided so as to divide said catalyst bed means into at least two catalyst beds which are not in direct communication with each other and have substantially sectorial horizontal cross sections, said at least two catalyst beds being defined by a plurality of radially extending vertical partition walls which extend in different radial directions in said intercylinder space, and wall means for directing the gaseous feed materials to flow in series through said at least two catalyst beds and to flow in a radial direction through each of said at least two catalyst beds.

6. A reactor as claimed in claim 5, further comprising means for allowing communication between said cooling tubes installed in the same one of each of said at least two catalyst beds to form a single cooling zone in each of said at least two catalyst beds, each of said cooling zones having separate coolant inlet and coolant outlet passages associated therewith.

7. A reactor as claimed in claim 5 wherein said cooling passage structure does not extend through one of said at least two catalyst beds.

9. A reactor as claimed in claim 2 or claim 4 wherein said at least one coolant distributing header and said at least one coolant collecting header are substantially tubular members.

11. A reactor as claimed in claim 2 or claim 4, wherein said cooling passage structure comprises a duplex pipe which extends through said top cover of said outer pressure vessel, said duplex pipe comprising an inner pipe and an outer pipe positioned and arranged to define an annular space therebetween, the interior of said inner pipe comprising said coolant inlet passage means and the annular space between said inner and outer pipes defining said coolant outlet passage means, said inner pipe penetrating to a location near said bottom wall beneath said catalyst bed means at which location said inner pipe communicates with said at least one distributing header which distributes the coolant to the bottom ends of said tubes, under pressure, and after the coolant passes upwardly through said tubes and is heated by heat exchange with said catalyst bed means to form coolant vapor, the coolant vapor is collected in said at least one collecting header which communicates directly with said coolant outlet passage.

12. A reactor as claimed in claim 2 or claim 4 wherein said grannular catalyst bed means is a single annular catalyst bed.

13. A reactor as claimed in claim 12, in which said at least one coolant distributing header is a single distributing header and said at least one coolant collecting header is a single collecting header, the upper ends of all of said cooling tubes are connected to said signle collecting header and the lower ends of all of said cooling tubes are connected to said single distributing header so that said cooling tubes form a single cooling zone in said annular catalyst bed.

14. A reactor as claimed in claim 12, in which said at least one coolant distributing header comprises at least two distributing headers and said at least one coolant collecting header comprises at least two collecting headers, said cooling tubes are separated into at least two separate groups which are not in communication with each other, the lower ends of said cooling tubes of each group being connected to a single one of said at least two distributing headers and the upper ends of said cooling tubes of each group being connected to a single one of said at least two collecting headers, whereby said groups form at least two cooling zones that occupy different radial portions of said annular catalyst bed, each of said groups of cooling tubes having separate coolant outlet and coolant inlet passages connected thereto.

4. A reactor for effecting a catalytic reaction wherein pressurized gaseous feed materials containing hydrogen contact a granular catalyst at an elevated temperature to form a high temperature reaction product gas, said reactor comprising:

a cylindrical, vertical, outer, pressure vessel having a top cover, a bottom cover, an inlet for the gaseous feed materials and an outlet for the reaction product gas;

a shell-and-tube heat exchanger centrally mounted within said outer pressure vessel and coaxial therewith, said heat exchanger comprising a vertically mounted cylindrical outer shell, upper and lower partition plates inside said shell defining the upper and lower ends of a shell-side heat exchange compartment therein and also defining upper and lower chambers within said heat exchanger which upper and lower chambers do not communicate with said compartment and a plurality of heat exchange tubes which penetrate said partition plates and extend into and through said compartment but do not communicate therewith, said heat exchanger having a heat transfer area sufficient to preheat low temperature gaseous feed materials and to cool the high temperature reaction product gas to a temperature below 300°

C., by flowing the gaseous feed materials and the reaction product gas in indirect heat exchanging relationship in said heat exchanger;

inner and outer, coaxial, cylindrical, gas-permeable, catalyst retainers, said catalyst retainers being mounted within said pressure vessel coaxially therewith and located between said shell of said heat exchanger and said pressure vessel, said inner and outer catalyst retainers positioned so as to define an annular intercylinder space;

a bottom wall extending beneath said catalyst retainers and fixedly connecting said catalyst retainers to each other;

granular catalyst bed means packed in the intercylinder space between said catalyst retainers above said bottom wall;

first feed gas passage means for conducting the gaseous feed materials to said heat exchange tubes of said heat exchanger, and second feed gas passage means for introducing preheated gaseous feed materials discharged from said heat exchange tubes of said heat exchanger into said catalyst bed means and flowing the preheated gaseous feed materials radially through said catalyst bed means;

first reaction product gas passage means for conducting the high temperature reaction product gas discharged from said catalyst bed means to said shell-side heat exchange compartment for indirect heat exchange interaction with the gaseous feed materials whereby to cool the reaction product gas and to heat the gaseous feed materials;

second reaction product gas passage means for receiving the cooled reaction product gas discharged from said shell-side heat exchange compartment of said heat exchanger;

a cooling passage structure for indirectly cooling the contents of said catalyst bed means by passing a liquid coolant therethrough, the liquid coolant having a boiling point temperature which permits the liquid coolant to boil when subjected to an elevated temperature and pressure, said coolant passage structure comprising coolant inlet passage means and coolant outlet passage means both extending through said top cover of said outer pressure vessel, at least one coolant distributing header for receiving coolant from said coolant inlet passage means and at least one coolant collecting header for supplying coolant to said coolant outlet passage means and a multiplicity of vertical cooling tubes which extend vertically within said catalyst bed means, said cooling tubes being arranged in at least one arcuate formation concentric with the vertical axis of said outer pressure vessel, the lower end of each of said cooling tubes being connected with said coolant inlet passage means by said at least one coolant distributing header and the upper end of each of said cooling tubes being connected with said coolant outlet passage means by said at least one coolant collecting header so that the coolant may be circulated through said cooling passage structure, said coolant inlet passage means supplying the liquid coolant to the lower ends of said cooling tubes by said at least one distributing header and said coolant outlet passage means discharging vapor of the coolant or a liquid-vapor mixture of the coolant collected by said at least one collecting header from the upper ends of said cooling tubes; and

a cylindrical, gas-impermeable, outer, partition wall having a heat insulating layer thereon, said gas-impermeable outer partition wall being mounted coaxially within said pressure vessel and being located between and spaced from said pressure vessel and said outer, gas-permeable, catalyst retainer, said cylindrical outer partition wall being positioned and arranged so as to define a first elongated passageway between said pressure vessel and said cylindrical outer partition wall and defining a second elongated passageway between said cylindrical outer partition wall and said outer catalyst retainer, which first and second passageways are not in direct communication with each other, one end of said first passageway being in direct communication with said outlet for the product gas, the other end of said first passageway being connected to said second reaction product gas passage means so that the cooled reaction product gas discharged from said heat exchanger flows into and through said first passageway, said second passageway being connected with said first reaction product gas passage means for directing the high temperature reaction product gas discharged from said catalyst bed means into said shell-side heat exchange compartment of said heat exchanger.

8. A reactor as claimed in claim 4, wherein said coolant inlet and coolant outlet passages means comprises a duplex pipe which extends into said reactor through the top cover of said outer pressure vessel, said duplex pipe including an inner pipe and an outer pipe coaxially positioned and arranged to define an annular space, said coolant inlet, passage means comprising the interior of said inner pipe, and said coolant outlet passage means is defined by said annular space between said inner and outer pipes.

10. A reactor as claimed in claim 4, wherein each of said heat exchanger tubes is of spirally curved shape within said compartment of said heat exchanger.

15. In a reactor including an outer pressure vessel having an inlet passage for feeding gaseous feed materials into said pressure vessel and an outlet passage for discharging a product gas therefrom, a bed of a granular catalyst and means for flowing a reactant gas comprising the gaseous feed materials through said granular catalyst so that it reacts to form a product gas, means for cooling the product gas and preheating the gaseous feed materials, and means for cooling the reactant gas as the reactant gas passes through said catalyst bed, the improvement which comprises:

said outer pressure vessel is upright and cylindrical, and comprises a bottom cover and a removable top cover;

said cooling and preheating means comprises a heat exchanger centrally mounted within said outer pressure vessel coaxially therewith, said heat exchanger comprising a substantially cylindrical outer shell, upper and lower partition plates subdividing the interior of said shell in the lengthwise direction thereof, a plurality of heat exchanger tubes extending from said upper partition plate to said lower partition plate, said heat exchanger tubes opening above said upper partition plate and opening below said lower partition plate, said partition plates being positioned so as to define a shell-side heat exchange compartment therebetween, an upper chamber above said upper partition plate and a lower chamber below said lower partition plate, said shell of said heat exchanger having openings at opposite end portions thereof so that a gas can enter said compartment near one end of said compartment and be discharged from the opening at the other end of said compartment, said inlet passage for the gaseous feed materials being in communication with said heat exchanger tubes of said heat exchanger so that the gaseous feed materials undergo heat exchange and are thereby preheated before being fed to said catalyst bed;

said catalyst bed comprises spaced-apart inner and outer cylinder gas-permeable catalyst retainers being positioned and arranged so as to define an intercylinder space therebetween coaxial with said outer pressure vessel and said heat exchanger, said inner catalyst retainer being of smaller diameter than said outer catalyst retainer, and a bottom wall extending beneath said catalyst retainers and fixedly connecting said catalyst retainers to each other, said catalyst retainers and said bottom wall being spaced apart from the inner periphery of said outer pressure vessel, said granular catalyst being packed in the intercylinder space between said inner and outer catalyst retainers above said bottom wall;

said cooling means comprising a cooling structure having a coolant inlet passage and a coolant outlet passage which both extend through said top cover of said outer pressure vessel, and a multiplicity of vertical cooling tubes which extend through said catalyst bed, said granular catalyst being packed around said cooling tubes, each of said cooling tubes being in communication with said coolant inlet passage and said coolant outlet passage so that a liquid coolant may be circulated through said cooling structure to absorb reaction heat generated in said catalyst bed;

a cylindrical, gas-impermeable, outer, partition wall coaxial with said outer pressure vessel and located between said outer pressure vessel and said outer gas-permeable catalyst retainer and spaced therefrom so as to be positioned to define a first outer gas flow passageway between said outer pressure vessel and said cylindrical outer partition wall and a second inner gas flow passageway between said cylindrical outer partition wall and said outer catalyst retainer, whereby the product gas from said catalyst bed is discharged through said outer catalyst retainer into said second inner gas flow passageway, flows through said second inner flow passageway and thence into said shell-side heat exchange compartment of said heat exchanger, undergoes heat exchange with the gaseous feed materials in said heat exchanger, thereby cooling the product gas, and then is fed through said first outer gas flow passageway to the product gas outlet formed on said outer pressure vessel.