NOVELTY - Mixture for the treatment of liquid waste such as domestic waste water or slops, comprises: (i) two additives, 3.840 g of calcium hydroxide and 1.860 g of aluminum sulfate 30-mesh screening, respectively; (ii) a formulation consisting of a starch-paste and hydrated bentonite; and (iii) 1.2 kg of zeolite screened mesh 30.    USE - The mixture and methods are useful for the treatment of liquid waste such as domestic waste water or slops (claimed).    ADVANTAGE - The mixture and methods are environment friendly, and simultaneously uses zeolites and a starch gel or pre-gel, which results in a single gelling process using the material, mainly but not exclusively applied to hot vinasse.    DETAILED DESCRIPTION - Mixture for the treatment of liquid waste such as domestic waste water or slops, comprises: (i) two additives, 3.840 g of calcium hydroxide and 1.860 g of aluminum sulfate 30-mesh screening, respectively, and (ii) a formulation consisting of a starch-paste and hydrated bentonite, where the starch-paste is composed of the following parts: mix A consists of: (a) 60 g commercial basis cationic starch, (b) 40 g waxy starch commercial basis, (c) 150 ml of drinking water, (d) 1.5 g sodium chloride, (e) 1.0 ml of epichlorohydrin; solution B composed of: (a) 6.0 g potassium hydroxide, (b) 40 ml of water; and solution C consists of: (a) 20 g Xanthan Gum, (b) 2.060 ml of water, (c) 2.5 ml of Kathon LX; and the hydrated bentonite, is composed of: (a) 630 g commercial Bentonite, (b) 3.570 ml of water; and (iii) 1.2 kg of zeolite screened mesh 30. INDEPENDENT CLAIMS are:    (1) a method for preparing the mixture for treating liquid waste, where the vinasse is neutralized early in the process which comprises: (a) preparing the mix tank A and solution B separately; (b) add a solution ? in the mixture A, slowly over 30 minutes; (c) heating the dispersion to 50 degrees C; if an exothermic temperature rise, reaching 55 degrees C, cooled so that the dispersion temperature is in the range 55 degrees C not less than T not less than 60 degrees C; keeping the duration of the exothermic well, for at least 40 minutes if the exotherm is not presented, when the temperature drop spontaneously to 50 degrees C, or after 40 minutes; (d) adding the water of the C and heating at 50 degrees C, then slowly adding dispersing gum, keeping the temperature at 50 degrees C for 30 minutes; (e) raising the temperature up to 65 degrees C and keeping it there for 20 minutes; (f) cooling to room temperature (30 degrees C preferred) and adding 2.5 ml of Kathon LX; (g) obtaining 2.381 g or 2.334 g of mixture in my; (h) cross-linking a mixture of three parts of cationic starch with two parts of Waxy starch (Waxysol 2030); (i) grafting the cross-linked xanthan gum, thus generating the starch-paste; and (j) adding to the mixture of the starches, these zeolites to absorb them;    (2) a method of obtaining a mixture of optional vinasse treatment or wastewater;    (3) mix vinasse for treating sewage comprising: (a) 30.77% cross-linked starch, (b) bentonite 46.15%; (c) 15.38% of silicon dioxide; and (d) 7.69% of xanthan gum;    (4) a process for the treatment of liquid waste such as sewage vinasse or domestic use, comprising: (I) transporting the tequila process resulting stillage using conventional pipe bomb of the drives to a first collection tank; (II) storing the vinasse to a temperature of between 60-90 degrees C which is the average temperature leaving the tequila manufacturing process; this method of treatment of vinasses operates more efficiently when the temperature is 90 degrees C, promptly for inflow vinasse, the inlet pipe is provided with a first valve located near the upper edge of the tank, which regulates the amount of incoming vinasse also in this upper area is located a cap, which while avoiding spills, hermetically closes the collection tank, thus reducing the temperature loss in the vinasse; it is important that this process can optionally operate vinasse cold, i.e. at a temperature of between 10 and 20 degrees C, it is necessary to allow to react twice as long to obtain the deproteinization effect of the reagent mixture with the bentonite; output of vinasse collection tank has an outlet pipe located at its bottom to go through gravity stillage tank; this output regulates its flow through a second valve; (III) transporting vinasse called to a second reaction tank, which has: an inlet pipe that connects to the outlet pipe collection stillage tank, an engine equipped with a start button and a stop, a propeller stirrer, which rotates between 19 and 21 rpm to assure that no floc breakage in addition to the correct homogenization of the mixture, since inside the reaction tank besides vinasses, are introduced by means of a gate additives (oxides of calcium, aluminum and magnesium) and a formulation, the latter consisting of: a starch composed of rubber encapsulated in zeolite and bentonite do hydrated; an outlet pipe vinasse treated, located in the lower area of the reaction tank, the flow is regulated vinasse treated through a valve; and (IV) carrying treated stillage from the reaction tank, to a section of pipe that has a pump, which drives the vinasse treated to a settler or a centrifuge, separating acting vinasse treated. The pipe section ends in a triple router, which will connect three pipes, which via their respective valves allow the flow of treated vinasses; the first line re-enters the stillage to reaction tank, same account at the top with an inlet pipe for it; it is important for reentry of vinasse two pipes are closed, once the re was held batch circulation of 400 L, the first pipe is closed to enable the flow through vinasse, the second pipe leads the vinasse treated to a precipitation tank sludge same is equipped with a tank for collection of sludge and the third pipe that carries water resulting from vinasse treated to a treatment tank, where the added enzymatic and bacterial products; finally, the treatment tank 6 is transferred resulting water until a pair of filters, the features of the first and second filter charcoal zeolites have the degree cleaned water to make it potable; and    (5) a formulation for treating liquid waste such as domestic water vinasse or characterized by comprising amylose and amylopectin in various proportions, preponderantly by any of both substances as well as natural or synthetic zeolites and any starch added bentonite.