1. A process for desalination and byproduct processing utilizing renewable thermal energy input comprising: a) Utilizing thermal energy converted to at least one of rotational work and electricity for at least one sub-process and module; b) Input of recycled brine solution to at least one evaporator module; c) Input of pre-heat and heat thermal energy to said at least one evaporator module; d) Recovering waste heat from said at least one evaporator module using at least one waste-heat recovery loop; e) Wherein said at least one byproduct from said at least one evaporator module is input to at least one vacuum evaporation module; f) Combining said at least one byproduct from said at least one evaporator module transferred to said at least one vacuum evaporation module with raw materials and thermal energy input; g) Recovering waste heat from said vacuum evaporation module using at least one waste-heat recovery loop; h) Processing materials from said at least one vacuum evaporation module through at least one camalite crystallization module; i) Wherein byproduct from said at least one camalite crystallization module is processed through at least one of a bromide stripper and absorber module and a leaching module; j) Wherein materials from said leaching module are processed through at least one filter-dehydrator module; k) Wherein materials from said at least one filter-dehydrator module are processed through at least one hydrator-electrolyzer module; l) Wherein materials from said at least one camalite crystallization module transferred to at least one bromide stripper and absorber module are combined with raw materials and thermal energy input; m) Recovering waste heat from said at least one bromide stripper and absorber module using at least one waste-heat loop; n) Processing materials from said at least one bromide stripper and absorber module to at least one of a distillation module and precipitation module; o) Processing materials from said distillation module to a bromide production module; p) Wherein materials from said at least one bromide stripper and absorber module transferred to at least one precipitation module are combined with raw materials and thermal energy input; q) Recovering waste heat from said at least one precipitation module using at least one waste-heat loop; r) Processing materials from said at least one precipitation module to at least one filter-washing module; s) Processing materials from said at least one filter-washing module to at least one of a dryer module and ammonia loop module; and t) Wherein said at least one ammonia loop module transfers materials back to said at least one precipitation module.