Sulfate-Rich Saline Stream De-scaling via Precipitation
Find Innovative SolutionsGenerate Solutions
Solution Overview
Problem
Conventional methods for treating produced water from oil fields are inefficient and costly due to the presence of radioactive alkaline earth cations and sulfate-rich streams, which pose handling hazards and limit the effectiveness of desalination processes in seawater and oil-gas fields.
Innovation Solution
A method for separating magnesium as brucite and sulfate as calcium sulfoaluminate or calcium sulfoferrate from sulfate-rich saline streams, allowing for de-scaling and de-salting, which enhances desalination efficiency and enables the reuse of treated water in oil-gas fields or as a feedstock for chlor-alkali industries.
Engineering Contradictions & Design Principles
Engineering Contradiction Analysis
1Reliability
If conventional de-oiling and desalination methods are used on produced water, then oil removal is achieved, but treatment cost increases substantially due to radioactive NORM and sulfate content
Solution Approach 1:
The treatment process is divided into distinct stages: first stage removes oil droplets greater than 100 microns using sludge catchers, second stage removes dispersed oil droplets greater than 15-20 microns using corrugated plate separators or hydrocyclones, and third stage polishes to remove oil contents of about 10 microns using induced gas flotation or adsorption. This segmentation allows each stage to target specific oil sizes efficiently
Solution Approach 2:
The patent extracts and removes radioactive NORM (strontium, barium, radium) and sulfate from produced water through specialized treatment processes before the conventional de-oiling stages, preventing these contaminants from interfering with subsequent treatment steps and reducing overall treatment complexity and cost
2Ease of manufacture
If produced water is directly disposed by re-injection without treatment, then treatment cost is minimized, but environmental and technical hazards arise from radioactive NORM
Solution Approach 1:
The patent converts the harmful radioactive NORM and sulfate contaminants into removable targets for treatment. By specifically targeting strontium, barium, radium, and sulfate through precipitation and filtration processes, the system transforms these hazardous substances into separable components that can be removed, allowing the treated water to be safely re-injected or reused
3Productivity
If multi-stage de-oiling processes are applied to produced water, then oil separation efficiency improves, but process complexity and operational cost increase
Solution Approach 1:
The patent applies preliminary action by removing radioactive NORM and sulfate from produced water before the conventional multi-stage de-oiling process. This pre-treatment prevents interference with subsequent oil separation stages, allowing each stage to operate more efficiently and reducing the need for excessive polishing steps
Applied Scientific Principles
This section explains which scientific principles are used to turn an abstract innovation direction into a practical engineering solution.
Function Achieved in This Case
This approach effectively de-scales sulfate-rich streams, improving the performance and cost-effectiveness of desalination processes, allowing for the safe handling and reuse of treated water, reducing radiation hazards, and increasing hydrocarbons recovery.
Implementation Method 1
separating magnesium as brucite
Implementation Method 2
separating sulfate as calcium sulfoaluminate
Implementation Method 3
Multi-Stage Flash (MSF) desalination process
Implementation Method 4
produce a distillate
Data Source
AI summary
The invention presents innovative methods to de-scale sulfate-rich saline streams such as seawater and the like in conjunction with desalination processes. The effective de-scaling of such streams by the inventive methods: (1) enhances the performance, efficiency and cost effectiveness of desalination processes; and (2) allows the viable use of the de-scaled reject brine from desalination processes, for example, as a suitable saline water for oil-gas field's water injection operations to improve hydrocarbons recovery and/or as a feed stock for chlor-alkali industries.


