Tag: Industrial
H2S and Sulfide Control for a Poultry Processing Facility Case Study
Reliability in the Face of Supply Chain Disruption
Acid Mine Drainage Treatment Case Study
Control of NOx Emissions in a Titanium Sheet Metal Pickling Bath
HNO2 + H2O<sub”>2 <sub”>→ HNO3 + H2O Wt. ratio: 0.4
2NO + 3H2O2 → 2HNO3 + 2H2O Wt. ratio: 1.7
As shown in the reactions above, oxidation of NOx by H2O2 in-bath, produces nitric acid, thereby allowing recovery and reuse of a critical process reagent. Solution After initial testing, a full-scale demo was put in place for several months on the coiler bath at the plant. USP’s turn-key supply scope included 50 percent technical grade H2O2, a 3,000 gallon double walled bulk storage and an automated feed system. The turn-key system was solely maintained by USP. The program also included USP’s ChemWatch™ – advanced control system with remote telemetry, allowing tank monitoring for inventory and pump systems control and analysis. The tank and pump system are located in the middle of the coil storage area. Since the delivery connection is outside of the building, the system employs a remote delivery alarm system. Results shown in Figure 1 demonstrates how after an initial high dose of H2O2 to treat the NOx that had already built up in the bath, the NOx emissions were effectively controlled with a steady feed rate of 5 gph. Read More Download Case Study_Pickling Bath-17-HR (pdf)REFINERY GRADE HYDROGEN PEROXIDE ELIMINATES HAZARDOUS HYDROGEN SULFIDE GAS RELEASES DURING COKER UNIT OPERATIONS
Project Scope
A gulf coast refinery was experiencing unacceptable hydrogen sulfide (H2S) releases into occupied work areas in the Coker unit during cutting & quenching operations. Refinery Coker units are used to process residual oil or ‘heavy ends’. A part of the coking process requires quenching the hot coke with water, resulting in latent hydrogen sulfide being transferred to the water stream and stripping into the vapor phase creating potential exposure risks to operations personnel. In order to protect worker s, hydrogen sulfides in the process water stream must be eliminated.
In late 2016, USP Technologies (USP), leaders in peroxygen-based technologies for industrial water and wastewater treatment applications, was contacted by the refinery in search of a viable solution for its H2S issues. USP recommended a full-service chemical treatment program which included 27% refinery grade hydrogen peroxide, chemical storage, a dosing equipment system, inventory analysis, logistics management, safety training and ongoing field and technical support.
Full-Service Hydrogen Peroxide Treatment Program
The refinery recycles coker quench water in a closed loop, where any chemical used for treatment cannot negatively impact the coking process. Under near neutral pH conditions, the theoretical weight ratio of H2O2:H2S is 1:1, and proceeds according to the following reaction:
H2O2 + H2S → S0 + 2 H2O
Since the products of the above reaction are water and inactive elemental sulfur, the chemistry does not negatively impact the batch coking process.
Read More Download Case Study_Refinery Coker Quenchwater-18-HR (pdf)[/vc_column_text][/vc_column][/vc_row]Odor and Corrosion Best Practices Webinar
City of Wichita, Kansas’ Odor Control Program – Continuing Optimization with a Cost-Conscious Approach
ABSTRACT
This paper describes the evolving odor control program of the City of Wichita, Kansas from 2008 to 2015. In 2010, the City reduced odor control technology expenditure due to a reduction of revenues. The odors increased resulting in an upswing in citizen complaints as well as more corrosion in existing plant and lift station equipment. In 2013, the City re-evaluated their existing technology approaches to odor control and implemented optimized chemical dosing strategies to maximize cost-effectiveness and provide wide-ranging benefits. USP Technologies (USP) partnered with the City to implement state of the art chemical dosing controls to efficiently target sulfides with their hydrogen peroxide (H2O2) and peroxide regenerated iron sulfide control (PRI-SC®) treatment programs. Implementing the proper treatment technology and chemical dosing controls resulted in dramatically reduced sulfide levels in both the liquid and gaseous phases while providing more cost-effective treatment.
KEYWORDS
Odor control, cost-conscious approach, Wichita, hydrogen sulfide, PRI-SC®, peroxide regenerated iron – sulfide control, hydrogen peroxide, ferrous chloride, RFQ process, odor complaints, corrosion control
Read More Download Wichita – OAP 2016 (pdf) Download Wichita Odor Control PPT – OAP 2016 (pdf)[/vc_column_text][/vc_column][/vc_row]Temporary Phenol Oxidation Program to Support a Refinery Aeration Basin Turnaround – Lab Treatability Testing Through Successful Full Scale Implementation – A Case Study
ABSTRACT
In 2015, a maintenance turnaround of the wastewater aeration tank was undertaken at United Refining Company in Warren, PA. During the planned 70 day turnaround, the refinery needed a temporary chemical oxidation program to maintain compliance with permitted effluent phenol levels. This paper will present data and key learnings from all phases of this successful project, including laboratory treatability testing, process design, full scale implementation and successful completion.
KEYWORDS: Phenol, Aeration Basin, Oxidation, Permanganate, Dissolved Air Flotation (DAF), Total Suspended Solids (TSS)
Read More
Download United Refining Company – IWC 2016 (pdf)[/vc_column_text][/vc_column][/vc_row]Effective Collection System Sulfide and Corrosion Management Planning
ABSTRACT
This paper presents a systematic, step-by-step approach to assist utilities in developing an effective, priority-driven, sulfide and corrosion management plan for their collection systems. Along with aging infrastructure, utilities are faced with problems with high hydrogen sulfide and corrosion in their collection systems. One of the main challenges in addressing these concerns is developing a method to prioritize critical areas of concern for rehabilitation/replacement and/or corrosion treatment. The systematic approach presented herein provides a comprehensive means which includes six key steps as listed below:- Identification of potential Critical Areas of Concern (CAC) for corrosion
- Review of current schedule for Capital Improvements Projects (CIPs)
- Risk assessment of interceptor condition and risk rating of CAC
- Evaluation of odor control and corrosion treatment methods
- Rating of interceptor repair and replacement techniques
- Development of corrosion management program (CMP)