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$21 USD / hour
Flag of FINLAND
helsinki, finland
$21 USD / hour
It's currently 9:53 AM here
Joined December 28, 2023
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Hunain V.

@hunainvohra

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$21 USD / hour
Flag of FINLAND
helsinki, finland
$21 USD / hour
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Process Engineering, AutoCad/3D Model/Oil & Gas

Hello! I'm Hunain Vohra, an experienced engineer with a strong focus on the oil and gas sector. Over the past 14 years , I've honed my skills in various aspects of engineering, specializing in process engineering. My expertise extends to utilizing advanced engineering software to optimize processes and ensure reliability. What I offer: ✔️ Design and optimization of oil and gas processes, covering all stages from conceptualization to implementation. ✔️ Calculation, sizing, and validation of process parameters to ensure optimal performance. ✔️ Stress analysis and reliability engineering for piping systems to guarantee structural integrity. ✔️ Expertise in instrument and control engineering, ensuring precise monitoring and regulation. ✔️ Cost estimation to provide accurate project budgeting and resource planning. ✔️ Proficiency in engineering software such as Aspen HYSYS, Aspen Flare net, and Aspen for process engineering. ✔️ Mastery Autocad 2D/3D for P&IDs . Let’s Work Together!!! I prioritize clear communication, keeping clients engaged throughout the project journey. If you're in search of an experienced and dependable engineer to elevate your project to new heights, your search ends here. Let's chat about your project requirements and how I can play a role in your success. ? Let's connect and embark on a rewarding journey of growth and accomplishment together. Hunain Vohra
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Portfolio

11589369
This project Isometric were developed for one of the engineering design houses in Pakistan. Project is for Gas development and few skids isometrics were assigned to me for developments.
Preparation of Isometric from P&ID for Oil & Gas Project
This project Isometric were developed for one of the engineering design houses in Pakistan. Project is for Gas development and few skids isometrics were assigned to me for developments.
Preparation of Isometric from P&ID for Oil & Gas Project
This project Isometric were developed for one of the engineering design houses in Pakistan. Project is for Gas development and few skids isometrics were assigned to me for developments.
Preparation of Isometric from P&ID for Oil & Gas Project
11589359
Client requested to develop 3D model for Condensate Storage tanks , Inlet separator skid and Degasser Skid using the P&ID. Models developed using AutoCad 3D ensuring safe distances as per API , easy of operability , maintenance access and inline with P&ID.
Development of 3D Models from P&IDs
Client requested to develop 3D model for Condensate Storage tanks , Inlet separator skid and Degasser Skid using the P&ID. Models developed using AutoCad 3D ensuring safe distances as per API , easy of operability , maintenance access and inline with P&ID.
Development of 3D Models from P&IDs
Client requested to develop 3D model for Condensate Storage tanks , Inlet separator skid and Degasser Skid using the P&ID. Models developed using AutoCad 3D ensuring safe distances as per API , easy of operability , maintenance access and inline with P&ID.
Development of 3D Models from P&IDs
Client requested to develop 3D model for Condensate Storage tanks , Inlet separator skid and Degasser Skid using the P&ID. Models developed using AutoCad 3D ensuring safe distances as per API , easy of operability , maintenance access and inline with P&ID.
Development of 3D Models from P&IDs
11589350
This project was related to develop an excel sheet and apply formula from API for identifying change in initial pressure due to change in Temperature. The theme of project is to identify thermal expansion of Diesel
Thermal Expansion of Diesel Expansion on Loading arm line
This project was related to develop an excel sheet and apply formula from API for identifying change in initial pressure due to change in Temperature. The theme of project is to identify thermal expansion of Diesel
Thermal Expansion of Diesel Expansion on Loading arm line
This project was related to develop an excel sheet and apply formula from API for identifying change in initial pressure due to change in Temperature. The theme of project is to identify thermal expansion of Diesel
Thermal Expansion of Diesel Expansion on Loading arm line
11589343
The purpose of project is to calculate pressure drop for domestic LPG users. Aspen HYSYS V11 “Pipe Segment” has been used for hydraulic line sizing of the LPG Distribution network. The Beggs and Brill (1979) correlation has been used for Pressure Drop and Velocity calculations of the piping network. Based on the conditions specified in the IGEM standards, following conclusions drawn: 1. The line size for main inlet line and for branch line is sufficient and meets the criteria for velocity and the pressure required at the outlet for appliance (i.e. 25 mbar maximum) 2. The criteria defined for pressure drop across the piping (i.e. 10% of Operating pressure when pressure is > 42 mbar) is not met considering that the pressure drop to the farthest point (LF-119-COMN-BF1-RTL-005) is 39 mbar which is 11% of the operating pressure
Pressure Drop Calculation for Domestic LPG users
The purpose of project is to calculate pressure drop for domestic LPG users. Aspen HYSYS V11 “Pipe Segment” has been used for hydraulic line sizing of the LPG Distribution network. The Beggs and Brill (1979) correlation has been used for Pressure Drop and Velocity calculations of the piping network. Based on the conditions specified in the IGEM standards, following conclusions drawn: 1. The line size for main inlet line and for branch line is sufficient and meets the criteria for velocity and the pressure required at the outlet for appliance (i.e. 25 mbar maximum) 2. The criteria defined for pressure drop across the piping (i.e. 10% of Operating pressure when pressure is > 42 mbar) is not met considering that the pressure drop to the farthest point (LF-119-COMN-BF1-RTL-005) is 39 mbar which is 11% of the operating pressure
Pressure Drop Calculation for Domestic LPG users
The purpose of project is to calculate pressure drop for domestic LPG users. Aspen HYSYS V11 “Pipe Segment” has been used for hydraulic line sizing of the LPG Distribution network. The Beggs and Brill (1979) correlation has been used for Pressure Drop and Velocity calculations of the piping network. Based on the conditions specified in the IGEM standards, following conclusions drawn: 1. The line size for main inlet line and for branch line is sufficient and meets the criteria for velocity and the pressure required at the outlet for appliance (i.e. 25 mbar maximum) 2. The criteria defined for pressure drop across the piping (i.e. 10% of Operating pressure when pressure is > 42 mbar) is not met considering that the pressure drop to the farthest point (LF-119-COMN-BF1-RTL-005) is 39 mbar which is 11% of the operating pressure
Pressure Drop Calculation for Domestic LPG users
11589369
This project Isometric were developed for one of the engineering design houses in Pakistan. Project is for Gas development and few skids isometrics were assigned to me for developments.
Preparation of Isometric from P&ID for Oil & Gas Project
This project Isometric were developed for one of the engineering design houses in Pakistan. Project is for Gas development and few skids isometrics were assigned to me for developments.
Preparation of Isometric from P&ID for Oil & Gas Project
This project Isometric were developed for one of the engineering design houses in Pakistan. Project is for Gas development and few skids isometrics were assigned to me for developments.
Preparation of Isometric from P&ID for Oil & Gas Project
11589359
Client requested to develop 3D model for Condensate Storage tanks , Inlet separator skid and Degasser Skid using the P&ID. Models developed using AutoCad 3D ensuring safe distances as per API , easy of operability , maintenance access and inline with P&ID.
Development of 3D Models from P&IDs
Client requested to develop 3D model for Condensate Storage tanks , Inlet separator skid and Degasser Skid using the P&ID. Models developed using AutoCad 3D ensuring safe distances as per API , easy of operability , maintenance access and inline with P&ID.
Development of 3D Models from P&IDs
Client requested to develop 3D model for Condensate Storage tanks , Inlet separator skid and Degasser Skid using the P&ID. Models developed using AutoCad 3D ensuring safe distances as per API , easy of operability , maintenance access and inline with P&ID.
Development of 3D Models from P&IDs
Client requested to develop 3D model for Condensate Storage tanks , Inlet separator skid and Degasser Skid using the P&ID. Models developed using AutoCad 3D ensuring safe distances as per API , easy of operability , maintenance access and inline with P&ID.
Development of 3D Models from P&IDs
11589350
This project was related to develop an excel sheet and apply formula from API for identifying change in initial pressure due to change in Temperature. The theme of project is to identify thermal expansion of Diesel
Thermal Expansion of Diesel Expansion on Loading arm line
This project was related to develop an excel sheet and apply formula from API for identifying change in initial pressure due to change in Temperature. The theme of project is to identify thermal expansion of Diesel
Thermal Expansion of Diesel Expansion on Loading arm line
This project was related to develop an excel sheet and apply formula from API for identifying change in initial pressure due to change in Temperature. The theme of project is to identify thermal expansion of Diesel
Thermal Expansion of Diesel Expansion on Loading arm line
11589343
The purpose of project is to calculate pressure drop for domestic LPG users. Aspen HYSYS V11 “Pipe Segment” has been used for hydraulic line sizing of the LPG Distribution network. The Beggs and Brill (1979) correlation has been used for Pressure Drop and Velocity calculations of the piping network. Based on the conditions specified in the IGEM standards, following conclusions drawn: 1. The line size for main inlet line and for branch line is sufficient and meets the criteria for velocity and the pressure required at the outlet for appliance (i.e. 25 mbar maximum) 2. The criteria defined for pressure drop across the piping (i.e. 10% of Operating pressure when pressure is > 42 mbar) is not met considering that the pressure drop to the farthest point (LF-119-COMN-BF1-RTL-005) is 39 mbar which is 11% of the operating pressure
Pressure Drop Calculation for Domestic LPG users
The purpose of project is to calculate pressure drop for domestic LPG users. Aspen HYSYS V11 “Pipe Segment” has been used for hydraulic line sizing of the LPG Distribution network. The Beggs and Brill (1979) correlation has been used for Pressure Drop and Velocity calculations of the piping network. Based on the conditions specified in the IGEM standards, following conclusions drawn: 1. The line size for main inlet line and for branch line is sufficient and meets the criteria for velocity and the pressure required at the outlet for appliance (i.e. 25 mbar maximum) 2. The criteria defined for pressure drop across the piping (i.e. 10% of Operating pressure when pressure is > 42 mbar) is not met considering that the pressure drop to the farthest point (LF-119-COMN-BF1-RTL-005) is 39 mbar which is 11% of the operating pressure
Pressure Drop Calculation for Domestic LPG users
The purpose of project is to calculate pressure drop for domestic LPG users. Aspen HYSYS V11 “Pipe Segment” has been used for hydraulic line sizing of the LPG Distribution network. The Beggs and Brill (1979) correlation has been used for Pressure Drop and Velocity calculations of the piping network. Based on the conditions specified in the IGEM standards, following conclusions drawn: 1. The line size for main inlet line and for branch line is sufficient and meets the criteria for velocity and the pressure required at the outlet for appliance (i.e. 25 mbar maximum) 2. The criteria defined for pressure drop across the piping (i.e. 10% of Operating pressure when pressure is > 42 mbar) is not met considering that the pressure drop to the farthest point (LF-119-COMN-BF1-RTL-005) is 39 mbar which is 11% of the operating pressure
Pressure Drop Calculation for Domestic LPG users

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Experience

Engineering Manager

Gasco Engineering Services
Apr 2010 - Present
Responsible for managing a team of engineers, ensuring project timelines and budgets are met, and collaborating with cross-functional teams. Key responsibilities include project planning, resource allocation, technical leadership, and adherence to industry standards and safety protocols.

Education

Master in Electronic

University of Surrey, United Kingdom 2008 - 2009
(1 year)

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Engineering
Electronics
Mechanical Engineering
Chemical Engineering

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