The invention discloses a hydrocarbon continuous reforming process which comprises at least three reforming reactors and at least one catalyst regenerator, wherein the last reforming reactor is called a second reactor, and the reactors except the last reforming reactor are called first reactors. Reaction feeding is performed in series relative to conveyance of each of reforming reactors. Circular conveyance of a catalyst between the first reactor and the second reactors and the regenerator is performed in parallel, and conveyance of the catalyst between the first reactor and the regenerator is performed in series in a countercurrent manner. According to the process, each of the reactors can use a fresh high-activity catalyst and the flow of the catalyst is independently adjusted and changed as required, so that the activity of the catalyst can be fully exerted, the utilization ratio of the catalyst is improved, and the reforming conversion rate and the product yield are improved.