Water-miscible metal working fluids with reduced aerosol inhalation toxicity
A metalworking, water-miscible technology, used in the petroleum industry, lubricating compositions, etc., that can solve problems such as low lung toxicity and low unsaturation levels
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Embodiment 1
[0043] This example employs a product-to-product process with continuous addition of starter (CAOS), wherein the product tails (from butanol and propylene oxide / epoxide) are added to the reactor at the start of the batch process. Ethane is prepared by the CAOS method, the hydroxyl value is about 35 mg KOH / g), a mixture of ethylene oxide and propylene oxide is added to activate the catalyst, and after activation, the starter or initiator is continuously added to the reactor , while adding one or more alkylene oxides. A double metal cyanide (DMC) catalyst prepared according to US Patent No. 5,482,908 was used in all examples. 2500 grams of product tails were charged to a 20 kg reactor along with DMC catalyst (0.87 grams). The mixture was dehydrated under nitrogen at 130°C for 30 minutes under vacuum. The catalyst was activated with 125 grams of mixed epoxides (50% by weight propylene oxide, 50% by weight ethylene oxide) fed at 130°C. After the pressure in the reactor dropped ...
Embodiment 2
[0045] The steps described in Example 1 were repeated, except that the ratio of ethylene oxide / propylene oxide was 35 / 65, and the amount of n-butanol added was reduced to produce a polyether having a hydroxyl value of about 17 mg KOH / g. The number average equivalent weight of the obtained product was 3187 g / mol, the viscosity at 37.8°C was 2060 SUS, the cloud point (1%, in water) was 40°C, and the LC of 4 hours aerosol exposure 50 The concentration is greater than 5.38 mg / L.
Embodiment 3
[0047] A semi-batch process is used in which the alkylene oxide is added to the starter without a continuous starter feed. 5426 grams of a product similar to that described above in Example 1 and DMC catalyst (0.9 grams) were charged to the reactor. The mixture was dehydrated under nitrogen at 130°C for 30 minutes under vacuum. The catalyst was activated with 271 grams of mixed epoxides (50% by weight propylene oxide, 50% by weight ethylene oxide) fed at 130°C. After the pressure drop in the reactor confirmed catalyst initiation, propylene oxide (6204 g) and ethylene oxide (6204 g) were simultaneously added to the reactor within 5 hours to generate a compound with a hydroxyl number of about 10 mg KOH / g. Polyether. The product has a number average equivalent weight of 5968 g / mol, a viscosity of 5340 SUS at 37.8° C., a cloud point (1%, in water) of 56° C., and a LC of 4 hours of aerosol exposure. 50 The concentration is less than 5.9 mg / L.
[0048] As can be seen with refere...
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