The invention discloses a hydrocarbon continuous reforming technology which comprises the following steps: at least three reforming reactors and at least one catalyst regenerator are arranged, wherein the last reforming reactor is called as a second group of reactors, the reactors except the last reforming reactor are called as a first group of reactors, conveying of reaction feeds is serially performed relative to each reforming reactor, while circulation conveying of a catalyst between the first group of reactors and the regenerator as well as between the second group of reactors and the regenerator is performed in parallel, and conveying of the catalyst between the first group of reactors and the regenerator is serially performed along a forward flow. In the hydrocarbon continuous reforming technology, each group of reactors can use a fresh high-activity catalyst, can independently regulate and change the flow rate of the catalyst according to the needs, can fully exert the activity of the catalyst and increases the utilization ratio of the catalyst, the reforming conversion rate and the yield of a product.