Bypass Pipe

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The Experts below are selected from a list of 126 Experts worldwide ranked by ideXlab platform

Krishnaswamy Nandakumar - One of the best experts on this subject based on the ideXlab platform.

  • Optimal Design of Bypass Line for an Industrial-Scale 8-Leg Polyolefin Loop Reactor to Manage Slurry Dispersion Using Hydraulic and CFD Simulations
    Industrial & Engineering Chemistry Research, 2018
    Co-Authors: Rupesh K. Reddy, Abhijit Rao, Sameer Vijay, Erno Elovainio, Christof Wurnisch, Krishnaswamy Nandakumar
    Abstract:

    The pump power oscillation caused by slugs in slurry phase polymerization reactors limits production capacity. A Bypass line connecting two locations of a loop reactor is suggested in patent literature to dissipate slugs. The optimal design of such Bypass lines is studied through a hierarchy of modeling approaches applied to an industrial-scale reactor. In the design process, 1D hydraulic calculations guide the selection of optimal Bypass Pipe sizes to maximize slurry velocity. 2D CFD simulations provide data on slug dissipation processes. 3D simulations guide selection of optimal installation angle to maximize solid intake into the Bypass line. By combining these approaches, a Bypass line connecting the second and sixth legs by 6 in. Pipes at a 45° angle is found to be optimal for reactor considered here. Such designs achieves high slurry velocity in the Bypass line while maximizing slug dissipation, and the approach is applicable for other loop reactor configurations.

  • Optimal Design of Bypass Line for an Industrial-Scale 8‑Leg Polyolefin Loop Reactor to Manage Slurry Dispersion Using Hydraulic and CFD Simulations
    2018
    Co-Authors: Rupesh Reddy, Abhijit Rao, Sameer Vijay, Erno Elovainio, Christof Wurnisch, Krishnaswamy Nandakumar
    Abstract:

    The pump power oscillation caused by slugs in slurry phase polymerization reactors limits production capacity. A Bypass line connecting two locations of a loop reactor is suggested in patent literature to dissipate slugs. The optimal design of such Bypass lines is studied through a hierarchy of modeling approaches applied to an industrial-scale reactor. In the design process, 1D hydraulic calculations guide the selection of optimal Bypass Pipe sizes to maximize slurry velocity. 2D CFD simulations provide data on slug dissipation processes. 3D simulations guide selection of optimal installation angle to maximize solid intake into the Bypass line. By combining these approaches, a Bypass line connecting the second and sixth legs by 6 in. Pipes at a 45° angle is found to be optimal for reactor considered here. Such designs achieves high slurry velocity in the Bypass line while maximizing slug dissipation, and the approach is applicable for other loop reactor configurations

Rupesh K. Reddy - One of the best experts on this subject based on the ideXlab platform.

  • Optimal Design of Bypass Line for an Industrial-Scale 8-Leg Polyolefin Loop Reactor to Manage Slurry Dispersion Using Hydraulic and CFD Simulations
    Industrial & Engineering Chemistry Research, 2018
    Co-Authors: Rupesh K. Reddy, Abhijit Rao, Sameer Vijay, Erno Elovainio, Christof Wurnisch, Krishnaswamy Nandakumar
    Abstract:

    The pump power oscillation caused by slugs in slurry phase polymerization reactors limits production capacity. A Bypass line connecting two locations of a loop reactor is suggested in patent literature to dissipate slugs. The optimal design of such Bypass lines is studied through a hierarchy of modeling approaches applied to an industrial-scale reactor. In the design process, 1D hydraulic calculations guide the selection of optimal Bypass Pipe sizes to maximize slurry velocity. 2D CFD simulations provide data on slug dissipation processes. 3D simulations guide selection of optimal installation angle to maximize solid intake into the Bypass line. By combining these approaches, a Bypass line connecting the second and sixth legs by 6 in. Pipes at a 45° angle is found to be optimal for reactor considered here. Such designs achieves high slurry velocity in the Bypass line while maximizing slug dissipation, and the approach is applicable for other loop reactor configurations.

Abhijit Rao - One of the best experts on this subject based on the ideXlab platform.

  • Optimal Design of Bypass Line for an Industrial-Scale 8-Leg Polyolefin Loop Reactor to Manage Slurry Dispersion Using Hydraulic and CFD Simulations
    Industrial & Engineering Chemistry Research, 2018
    Co-Authors: Rupesh K. Reddy, Abhijit Rao, Sameer Vijay, Erno Elovainio, Christof Wurnisch, Krishnaswamy Nandakumar
    Abstract:

    The pump power oscillation caused by slugs in slurry phase polymerization reactors limits production capacity. A Bypass line connecting two locations of a loop reactor is suggested in patent literature to dissipate slugs. The optimal design of such Bypass lines is studied through a hierarchy of modeling approaches applied to an industrial-scale reactor. In the design process, 1D hydraulic calculations guide the selection of optimal Bypass Pipe sizes to maximize slurry velocity. 2D CFD simulations provide data on slug dissipation processes. 3D simulations guide selection of optimal installation angle to maximize solid intake into the Bypass line. By combining these approaches, a Bypass line connecting the second and sixth legs by 6 in. Pipes at a 45° angle is found to be optimal for reactor considered here. Such designs achieves high slurry velocity in the Bypass line while maximizing slug dissipation, and the approach is applicable for other loop reactor configurations.

  • Optimal Design of Bypass Line for an Industrial-Scale 8‑Leg Polyolefin Loop Reactor to Manage Slurry Dispersion Using Hydraulic and CFD Simulations
    2018
    Co-Authors: Rupesh Reddy, Abhijit Rao, Sameer Vijay, Erno Elovainio, Christof Wurnisch, Krishnaswamy Nandakumar
    Abstract:

    The pump power oscillation caused by slugs in slurry phase polymerization reactors limits production capacity. A Bypass line connecting two locations of a loop reactor is suggested in patent literature to dissipate slugs. The optimal design of such Bypass lines is studied through a hierarchy of modeling approaches applied to an industrial-scale reactor. In the design process, 1D hydraulic calculations guide the selection of optimal Bypass Pipe sizes to maximize slurry velocity. 2D CFD simulations provide data on slug dissipation processes. 3D simulations guide selection of optimal installation angle to maximize solid intake into the Bypass line. By combining these approaches, a Bypass line connecting the second and sixth legs by 6 in. Pipes at a 45° angle is found to be optimal for reactor considered here. Such designs achieves high slurry velocity in the Bypass line while maximizing slug dissipation, and the approach is applicable for other loop reactor configurations

Christof Wurnisch - One of the best experts on this subject based on the ideXlab platform.

  • Optimal Design of Bypass Line for an Industrial-Scale 8-Leg Polyolefin Loop Reactor to Manage Slurry Dispersion Using Hydraulic and CFD Simulations
    Industrial & Engineering Chemistry Research, 2018
    Co-Authors: Rupesh K. Reddy, Abhijit Rao, Sameer Vijay, Erno Elovainio, Christof Wurnisch, Krishnaswamy Nandakumar
    Abstract:

    The pump power oscillation caused by slugs in slurry phase polymerization reactors limits production capacity. A Bypass line connecting two locations of a loop reactor is suggested in patent literature to dissipate slugs. The optimal design of such Bypass lines is studied through a hierarchy of modeling approaches applied to an industrial-scale reactor. In the design process, 1D hydraulic calculations guide the selection of optimal Bypass Pipe sizes to maximize slurry velocity. 2D CFD simulations provide data on slug dissipation processes. 3D simulations guide selection of optimal installation angle to maximize solid intake into the Bypass line. By combining these approaches, a Bypass line connecting the second and sixth legs by 6 in. Pipes at a 45° angle is found to be optimal for reactor considered here. Such designs achieves high slurry velocity in the Bypass line while maximizing slug dissipation, and the approach is applicable for other loop reactor configurations.

  • Optimal Design of Bypass Line for an Industrial-Scale 8‑Leg Polyolefin Loop Reactor to Manage Slurry Dispersion Using Hydraulic and CFD Simulations
    2018
    Co-Authors: Rupesh Reddy, Abhijit Rao, Sameer Vijay, Erno Elovainio, Christof Wurnisch, Krishnaswamy Nandakumar
    Abstract:

    The pump power oscillation caused by slugs in slurry phase polymerization reactors limits production capacity. A Bypass line connecting two locations of a loop reactor is suggested in patent literature to dissipate slugs. The optimal design of such Bypass lines is studied through a hierarchy of modeling approaches applied to an industrial-scale reactor. In the design process, 1D hydraulic calculations guide the selection of optimal Bypass Pipe sizes to maximize slurry velocity. 2D CFD simulations provide data on slug dissipation processes. 3D simulations guide selection of optimal installation angle to maximize solid intake into the Bypass line. By combining these approaches, a Bypass line connecting the second and sixth legs by 6 in. Pipes at a 45° angle is found to be optimal for reactor considered here. Such designs achieves high slurry velocity in the Bypass line while maximizing slug dissipation, and the approach is applicable for other loop reactor configurations

Erno Elovainio - One of the best experts on this subject based on the ideXlab platform.

  • Optimal Design of Bypass Line for an Industrial-Scale 8-Leg Polyolefin Loop Reactor to Manage Slurry Dispersion Using Hydraulic and CFD Simulations
    Industrial & Engineering Chemistry Research, 2018
    Co-Authors: Rupesh K. Reddy, Abhijit Rao, Sameer Vijay, Erno Elovainio, Christof Wurnisch, Krishnaswamy Nandakumar
    Abstract:

    The pump power oscillation caused by slugs in slurry phase polymerization reactors limits production capacity. A Bypass line connecting two locations of a loop reactor is suggested in patent literature to dissipate slugs. The optimal design of such Bypass lines is studied through a hierarchy of modeling approaches applied to an industrial-scale reactor. In the design process, 1D hydraulic calculations guide the selection of optimal Bypass Pipe sizes to maximize slurry velocity. 2D CFD simulations provide data on slug dissipation processes. 3D simulations guide selection of optimal installation angle to maximize solid intake into the Bypass line. By combining these approaches, a Bypass line connecting the second and sixth legs by 6 in. Pipes at a 45° angle is found to be optimal for reactor considered here. Such designs achieves high slurry velocity in the Bypass line while maximizing slug dissipation, and the approach is applicable for other loop reactor configurations.

  • Optimal Design of Bypass Line for an Industrial-Scale 8‑Leg Polyolefin Loop Reactor to Manage Slurry Dispersion Using Hydraulic and CFD Simulations
    2018
    Co-Authors: Rupesh Reddy, Abhijit Rao, Sameer Vijay, Erno Elovainio, Christof Wurnisch, Krishnaswamy Nandakumar
    Abstract:

    The pump power oscillation caused by slugs in slurry phase polymerization reactors limits production capacity. A Bypass line connecting two locations of a loop reactor is suggested in patent literature to dissipate slugs. The optimal design of such Bypass lines is studied through a hierarchy of modeling approaches applied to an industrial-scale reactor. In the design process, 1D hydraulic calculations guide the selection of optimal Bypass Pipe sizes to maximize slurry velocity. 2D CFD simulations provide data on slug dissipation processes. 3D simulations guide selection of optimal installation angle to maximize solid intake into the Bypass line. By combining these approaches, a Bypass line connecting the second and sixth legs by 6 in. Pipes at a 45° angle is found to be optimal for reactor considered here. Such designs achieves high slurry velocity in the Bypass line while maximizing slug dissipation, and the approach is applicable for other loop reactor configurations