Processes for increasing hydrogen recovery are described. The processes use cold carbon dioxide-enriched product from the carbon dioxide recovery system to chill the hydrogen PSA feed stream. The carbon dioxide-enriched product stream comprises a supercritical carbon dioxide stream or a liquid carbon dioxide stream. The synthesis gas stream is typically chilled to a temperature in a range of 0? C. to 40? C. The temperature of the chilled synthesis gas stream is typically at least 10? C. lower than the temperature of the synthesis gas before chilling.

The present disclosure relates to the technical field of separation of boron isotopes, in particular to a device and method for cracking a boron trifluoride complex. The device for cracking the boron trifluoride complex includes a continuous feeding system, a rising film preheater, a falling film preheater, a boron trifluoride gas circulation pipeline, a separation chamber, a cracking tower, a gas-liquid separator, an impurity removal tower, and anisole storage tank. By employing a continuous feeding method, the device for cracking boron trifluoride complex shortens retention time of anisole at a high-temperature stage while ensuring a cracking rate of a boron trifluoride-anisole complex, reduces the thermal decomposition degree of anisole, maintains the purity of anisole, and greatly improves the utilization rate and production safety of anisole, thus ensuring continuous and stable production.

The present invention relates to a method of preparing a gas coolant for the direct cooling of a unit operation under a fixed heat load from its normal operating temperature (e.g., 300 F. and above) to a lower temperature (e.g., below 100 F.) in order to allow for maintenance or other non-routine work to be carried out in said unit operation.