Abstract: A continuous solid organic matter pyrolysis polygeneration system and method for using the system is disclosed. The pyrolysis polygeneration system mainly includes a processing system, a drying furnace, a pyrolysis furnace, a cooling furnace, a tail gas treatment system, and a gas treatment system and a protective gas circulation system cooperate with each other to realize the multi-level rational utilization of energy, and are suitable for the continuous and rapid pyrolysis and carbonization of various solid organic matter in the actual production. While realizing the polygeneration of coke, wood vinegar and tar, the maximum utilization of overall heat is realized through process optimization.

Abstract: A method for flow control may include obtaining a number of added receive buffers based on adding receive buffers to a shared receive queue, obtaining initiators each including a protocol data unit (PDU) window size, obtaining a number of active initiators based on determining whether each of the initiators is associated with an active network session, calculating a credit using the number of added receive buffers and the number of active initiators, determining that an initiator is associated with an active network session, and adjusting the PDU window size of the initiator using the credit.