Deinking agent
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production example 1-1
[0048] To a 2-liter autoclave were charged 230.3 g of glycerin and 16.8 g of 100% KOH, and then the mixture was heated up to a temperature of 135.degree. C at a stirring rate of about 600 rpm. Next, the reaction mixture was caused to react with 1753 g of a mixture wherein the mole ratio between EO and PO was 228:102 (10 moles of EO and 4.5 moles of PO corresponding to one mole of glycerin). About reaction conditions at this time, the temperature was 135.degree. C. and the pressure was from 1 to 3 kg / cm.sup.2 (98 to 294 kPa) (gauge pressure). After the end of the reaction, the temperature was cooled to 80.degree. C. to yield an intermediate synthesis product 1 (reactant wherein 10 moles of EO and 4.5 moles of PO corresponded to one mole of glycerin).
[0049] Next, 290 g of the intermediate synthesis product 1 was charged into a 2-liter autoclave, and then the mixture was heated up to a temperature of 135.degree. C. at a stirring rate of about 600 rpm. The resultant was then caused to r...
production example 1-2
[0051] To a 2-liter autoclave was charged 668 g of the intermediate synthesis product 2 synthesized in Production Example 1-1, and then the mixture was heated up to a temperature of 135.degree. C. at a stirring rate of about 600 rpm. The resultant was then caused to react with 1311 g of a mixture wherein the mole ratio between EO and PO was 228:102. About reaction conditions at this time, the temperature was 135.degree. C. and the pressure was from 1 to 3 kg / cm.sup.2 (98 to 294 kPa) (gauge pressure). After the end of the reaction, the temperature was cooled to 80.degree. C. to yield an intermediate synthesis product 3 of AV=-0.3, OHV=16.3 and SV=-0.38 (reactant wherein 228 moles of EO and 102 moles of PO corresponded to one mole of glycerin).
[0052] Next, to a 200-mL four-neck flask were charged 136.8 g of the resultant intermediate synthesis product 3 and 13.2 g of stearic acid (AV=202.7) in such a manner that the mole ratio between the two, which was calculated from the OHV of the ...
production example 1-3
[0053] To a 2-liter autoclave were charged 151.1 g of tallow, 4.8 g of glycerin (0.3 mole of glycerin per mole of tallow) and 1.2 g of 100% KOH, and then the mixture was heated up to a temperature of 135.degree. C. at a stirring rate of about 600 rpm. Next, the reaction mixture was caused to react with 1834.4 g of a mixture wherein the mole ratio between EO and PO was 148:66 (148 moles of EO and 66 moles of PO corresponding to one mole of tallow). About reaction conditions at this time, the temperature was 135.degree. C. and the pressure was from 1 to 3 kg / cm.sup.2 (98 to 294 kPa) (gauge pressure). After the end of the reaction, the temperature was cooled to 80.degree. C. to yield a synthesis product (reactant wherein 148 moles of EO and 66 moles of PO corresponded to one mole of tallow, No. 17 of Table 1) wherein AV=0.52, OHV=18.9, SV=16.7 and the OHV / (SV-AV+OHV) was 0.54.
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