Water-miscible metal working fluids with reduced aerosol inhalation toxicity
a metal working fluid and aerosol inhalation technology, applied in the direction of liquid carbonaceous fuels, lubricant compositions, fuels, etc., can solve the problems of metal worker inhalation risk, metalworking operation nature, and possible respiratory problems
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example 1
[0038] This example employed a product-to-product process together with continuous addition of starter (CAOS), in which a heel of product (prepared from butanol and propylene oxide / ethylene oxide to a hydroxyl number of about 35 mg KOH / g via a CAOS process) was added to the reactor at the beginning of the batch, a mixture of ethylene oxide and propylene oxide was added to activate the catalyst, and an initiator or starter was fed continuously to the reactor simultaneously with the alkylene oxide or oxides after activation. Double metal cyanide (DMC) catalyst prepared according to U.S. Pat. No. 5,482,908 was used in all examples. A heel of 2,500 g of product was added to a 20 kg reactor along with DMC catalyst (0.87 g). The mixture was dehydrated with vacuum and nitrogen for 30 minutes at 130° C. The catalyst was activated with 125 g of mixed oxide (50 wt. % propylene oxide, 50 wt. % ethylene oxide) fed at 130° C. After the pressure drop in the reactor confirmed catalyst initiation, ...
example 2
[0039] The procedure described above in Example 1 was repeated, except the ethylene oxide / propylene oxide ratio was 35 / 65, and the amount of n-butanol fed was reduced to produce a polyether with a hydroxyl number of about 17 mg KOH / g. The resulting product had a number average equivalent weight of 3,187 g / mol, a viscosity of 2,060 SUS at 37.8° C., a cloud point (1% in water) of 40° C., and an LC50 concentration of >5.38 mg / L for a four-hour aerosol exposure.
example 3
[0040] A semi-batch process, in which alkylene oxides are added to an initiator without the presence of a continuous starter feed was used. The reactor was charged with 5,426 g of product similar to that described in Ex. 1 above together with DMC catalyst (0.9 g). The mixture was dehydrated with vacuum and nitrogen for 30 minutes at 130° C. The catalyst was activated with 271 g of mixed oxide (50 wt. % propylene oxide, 50 wt. % ethylene oxide) fed at 130° C. After the pressure drop in the reactor confirmed catalyst initiation, propylene oxide (6,204 g) and ethylene oxide (6,204 g) were added to the reactor simultaneously over a five-hour period to produce a polyether with a hydroxyl number of about 10 mg KOH / g. This product had an number average equivalent weight of 5,968 g / mol, a viscosity of 5,340 SUS at 37.8° C., a cloud point (1% in water) of 56° C., and an LC50 concentration <5.9 mg / L for a four-hour aerosol exposure.
[0041] As can be appreciated by reference to Table I below, ...
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