The process involves (a) continuously forming bromine chloride from separate feed streams of bromine and chlorine by maintaining said streams under automatic feed rate control whereby the streams are continuously proportioned to come together in equimolar amounts to form bromine chloride; (b) continuously forming an aqueous product having an active bromine content of at least 100,000 ppm (wt/wt), a pH of at least 7, and an atom ratio of nitrogen to active bromine greater than 0.93:1 by continuously feeding into mixing apparatus separate feed streams of (1) bromine chloride formed in (a), and (2) an aqueous solution of alkali metal salt of sulfamic acid, under automatic feed rate control whereby the feed streams are continuously proportioned to come together in amounts that produce an aqueous product having an active bromine content of at least 100,000 ppm (wt/wt), a pH of at least 7, and an atom ratio of nitrogen to active bromine from (1) and (2) greater than 0.93:1; and, (c) withdrawing said aqueous product from said mixing apparatus at a rate sufficient to enable the continuous feeding in (a) and (b) to be maintained.
该过程涉及(a)通过保持
溴和
氯的分开进料流,并通过维持所述流在自动进料速率控制下,连续形成
溴氯化物,使得这些流以等摩尔量连续配比在一起形成
溴氯化物;(b)通过不断向混合设备进料分开的(1)在(a)中形成的
溴氯化物和(2)
磺酸氨盐的碱
金属盐的
水溶液,使得进料流在自动进料速率控制下,不断配比在一起,产生具有至少100,000 ppm(重量/重量)活性
溴含量、至少7的pH值和氮原子与活性
溴之比大于0.93:1的
水溶液产品;以及(c)以足以使得在(a)和(b)中连续进料的速率维持的速率从所述混合设备中撤出所述
水溶液产品。