Methods and systems of operating a pump at an efficiency point during an in-line blending operation. In an embodiment, such a method may include transporting a fluid from a tank to a pump through a first pipe. The method may include discharging, via the pump, the fluid at a specified flow rate through a second pipe. The method may include measuring a flow rate of the first portion of the fluid flowing from the main control valve through the mixing pipe. The method may include measuring a flow rate of the second portion of the fluid flowing through the spillback loop. The method may include determining a current pump efficiency point and operating the pump within a range of percentages of the best efficiency point.

A system for mixing acid and water can include a tank for holding acid, an acid pump for pumping acid out of the tank, an acid flow meter, an acid control valve, a water pump for pumping water, a water flow meter, a water control valve, a flush valve to selectively flush the system with water, and a controller to monitor the flow meters and control the pumps and the valves. The acid control valve and/or the water control valve can be an electronically controlled valve. The flush valve can be an electronically controlled valve to selectively permit water to flow from downstream of the water pump to upstream of the acid pump. The acid control valve, the water control valve, the flush valve, or any combination thereof can be throttled by the controller to control flow therethrough.

Methods and systems of admixing hydrocarbon liquids from a plurality of tanks into a single pipeline thereof. The system may include two or more tanks positioned at a tank farm each containing a hydrocarbon liquid therein. The system may include two or more first main pipes, each connected to one of the tanks. The system may include two or more main valves, each connected to one of the first main pipes. The system may include two or more second main pipes each connected to a corresponding main valve. The system may include two or more mixing jumpers, each connected to a corresponding first main pipe, each mixing jumper to, when a corresponding main valve is closed, control hydrocarbon liquid. The system may include a mixing pipe, connected to the second main pipes and the mixing jumpers, configured to transport hydrocarbon liquid from one or more of the tanks.

The device for adjusting the concentration of a gas in a liquid includes a cartridge in which the concentration of the gas in the liquid is adjusted, a pipe for supplying the liquid into the cartridge, a pipe for supplying gas into the cartridge, and a pipe for discharging the liquid from the cartridge. The gas supply pipe includes an expansion valve with of which the pressure setpoint that is controlled by a setpoint for the quantity amount of gas in the liquid and by an amount of a quantity of gas in the liquid measured by a gas concentration sensor located in the liquid discharge pipe.

Bleach dilution and delivery vehicles are enabled. For example, a method can comprise: transporting, using a bleach dilution and delivery vehicle, sodium hypochlorite from a first location to a second location, mixing, using the bleach dilution and delivery vehicle, water from the second location and sodium hypochlorite from the bleach dilution and delivery vehicle to a defined strength, resulting in a diluted mix, and dispensing, using the bleach dilution and delivery vehicle, the diluted mix to the second location.

Bleach dilution and delivery vehicles are enabled. For example, a method can comprise: transporting, using a bleach dilution and delivery vehicle, sodium hypochlorite from a first location to a second location, mixing, using the bleach dilution and delivery vehicle, water from the second location and sodium hypochlorite from the bleach dilution and delivery vehicle to a defined strength, resulting in a diluted mix, and dispensing, using the bleach dilution and delivery vehicle, the diluted mix to the second location.

Methods and systems for producing ammonia, urea, and UAN are described herein. The methods can include providing a hydrocarbon feed stock and an oxygen-containing stream and reacting the hydrocarbon feed stock with the oxygen-containing stream to provide a syngas containing carbon dioxide and blue hydrogen. The methods can also include electrolyzing water to provide green hydrogen and blending the blue hydrogen with the green hydrogen to provide a blended hydrogen. The blended hydrogen can be introduced to an ammonia synthesis system to provide an ammonia product, which can be further processed to provide urea and/or UAN. The ratio of green to blue hydrogen in the blended hydrogen can be based on available green credits.

An onsite system for generating a fumigant for use with foodstuffs comprising: an active fumigant vaporizing station comprising: a first water heater; a heat exchanger connectable to the first water heater to receive heated water therefrom, the heat exchanger being configured to receive, heat and vaporise active liquid fumigant entering into the heat exchanger via a fumigant inlet; and a fumigant outlet connected to the plate heat exchanger for delivering a stream of vaporised fumigant; a liquid diluent vaporizing station comprising: a second water heater; a shell and tube heat exchanger connectable to the second water heater to receive heated water therefrom, the shell and tube heat exchanger being configured to receive, heat and vaporise the liquid diluent entering into the shell and tube heat exchanger via a mixing liquid inlet; and a mixing liquid outlet connected to the shell and tube heat exchanger for delivering the vaporised diluent; and a mixing unit configured to receive and mix the vaporised fumigant from the fumigant outlet and the vaporized diluent liquid from the diluent liquid outlet; mixing of the vaporised fumigant and vaporised mixing liquid to deliver a vaporised fumigant mixture; and a mixing and control means at the mixing unit for mixing the vaporised fumigant and diluent at, or substantially at, a predetermined mixing ratio.

An inline gas/liquid infusion system featuring an electronic control logic and subsystem having a signal processor configured to: receive signaling containing information about a liquid pressure of an incoming liquid provided from a pump to an inline gas liquid absorption device and about a gas pressure of an incoming gas provided to the inline gas liquid absorption device; and determine corresponding signaling containing information to control the liquid pressure of the incoming liquid provided from the pump to the inline gas liquid absorption device in order to provide real time adjustable set point output levels of gas absorption in the inline gas liquid absorption device, based upon the signaling received.

A system for mixing acid and water can include a tank for holding acid, an acid pump for pumping acid out of the tank, an acid flow meter, an acid control valve, a water pump for pumping water, a water flow meter, a water control valve, a flush valve to selectively flush the system with water, and a controller to monitor the flow meters and control the pumps and the valves. The acid control valve and/or the water control valve can be an electronically controlled valve. The flush valve can be an electronically controlled valve to selectively permit water to flow from downstream of the water pump to upstream of the acid pump. The acid control valve, the water control valve, the flush valve, or any combination thereof can be throttled by the controller to control flow therethrough.