A water purification device, with a first pressure cylinder, a second pressure cylinder, a first cylinder block and a second cylinder block. The first pressure cylinder, the second cylinder block and the second pressure cylinder are arranged successively, and the second cylinder block is arranged inside the first cylinder block. The first pressure cylinder and the second pressure cylinder both are open at one end and formed with a first through-hole at the other end, and enclosed. The first cylinder block and the second cylinder block both are open at two ends and arranged in a shape of hollow cylinder. A water inlet, which is communicated with flow passages formed between the first cylinder block and the second cylinder block, is formed on the second cylinder block, and a water outlet pipe communicated with the first cylinder block is inserted into an outer wall of the second cylinder block.

The invention involves a scale collection device that is located within downflow reactor head for removing solids from feed streams to increase reactor operating cycle time without impact on effective reactor space for catalyst loading and reactor pressure drop. More particularly, a scale collection device is in an upper portion of a reactor vessel above a rough liquid distribution tray and a vapor-liquid distribution tray.

Provided are water treatment cartridges, in particular gravitational flow treatment cartridges, that include a flow restriction element.

The invention involves a scale collection device that is located within downflow reactor head for removing solids from feed streams to increase reactor operating cycle time without impact on effective reactor space for catalyst loading. More particularly, a filtering zone is located in an upper portion of a reactor vessel above a rough liquid distribution tray and a distribution tray.

The invention involves a scale collection device that is located within downflow reactor head for removing solids from feed streams to increase reactor operating cycle time without impact on effective reactor space for catalyst loading and reactor pressure drop. More particularly, a scale collection device is located in an upper portion of a reactor vessel above a rough liquid distribution tray and a vapor-liquid distribution tray.

The invention involves a scale collection device that is located within downflow reactor head for removing solids from feed streams to increase reactor operating cycle time without impact on effective reactor space for catalyst loading. More particularly, a filtering zone is located in an upper portion of a reactor vessel above a rough liquid distribution tray and a distribution tray.

The invention involves a scale collection device that is located within downflow reactor head for removing solids from feed streams to increase reactor operating cycle time without impact on effective reactor space for catalyst loading and reactor pressure drop. More particularly, a scale collection device is in an upper portion of a reactor vessel above a rough liquid distribution tray and a vapor-liquid distribution tray.

The invention involves a scale collection device that is located within downflow reactor head for removing solids from feed streams to increase reactor operating cycle time without impact on effective reactor space for catalyst loading and reactor pressure drop. More particularly, a scale collection device is located in an upper portion of a reactor vessel above a rough liquid distribution tray and a vapor-liquid distribution tray.

A system includes a filtration vessel, a filtration input gauge, a filtration output gauge, a solvent vessel, an acid vessel, a water vessel, a computer, and a control system. The filtration vessel includes gravel configured to filter a produced water to create a filtered water. The filtration input gauge is configured to measure an inlet pressure of the produced water flowing into the filtration vessel. The filtration output gauge is configured to measure an outlet pressure of the filtered water flowing out of the filtration vessel. The computer is communicably connected to the filtration input gauge and the filtration output gauge and is configured to determine a differential pressure based on the inlet pressure and the outlet pressure. The control system is communicably connected to the computer and is configured to prevent the produced water from flowing to the filtration vessel and allow solvent, acid, and water to flow to the filtration vessel when the computer determines the differential pressure is greater than a pre-determined value.