Disclosed is a method for recovering phenol and acetone from the cracking reaction product of bisphenol-A residue, by which economic feasibility and efficiency may be improved by utilizing a phenol/acetone purification process used for preparing bisphenol-A.

Disclosed is a method for recovering phenol and acetone from the cracking reaction product of bisphenol-A residue, by which economic feasibility and efficiency may be improved by utilizing a phenol/acetone purification process used for preparing bisphenol-A.

Disclosed is a method for preparing acetaldehyde from acetylene under the catalysis of a ZAPO molecular sieve. The method comprises the steps of pre-heating an acetylene raw material gas and water, subjecting same to continuous hydration in a fluidized bed under the catalysis of the ZAPO molecular sieve to prepare acetaldehyde, and then subjecting same to separation, absorption and rectification to obtain an acetaldehyde product, wherein the catalyst can be continuously regenerated for use. The process of the present application is simple, stable and efficient, solves the problem of the dependence nature of the production of acetaldehyde by means of acetylene hydration on a mercury catalyst, avoids the harm caused by mercury to the human body and the environment, and has higher production and use values.

Disclosed is a method for preparing acetaldehyde from acetylene under the catalysis of a ZAPO molecular sieve. The method comprises the steps of pre-heating an acetylene raw material gas and water, subjecting same to continuous hydration in a fluidized bed under the catalysis of the ZAPO molecular sieve to prepare acetaldehyde, and then subjecting same to separation, absorption and rectification to obtain an acetaldehyde product, wherein the catalyst can be continuously regenerated for use. The process of the present application is simple, stable and efficient, solves the problem of the dependence nature of the production of acetaldehyde by means of acetylene hydration on a mercury catalyst, avoids the harm caused by mercury to the human body and the environment, and has higher production and use values.

The present invention relates to a process for preparing (Z)-7-tetradecen-2-one of the following formula (5), the process comprising the steps of converting a (Z)-1-halo-4-undecene compound (1) of the following general formula (1), wherein X.sup.1 represents a halogen atom, into a nucleophilic reagent, (Z)-4-undecenyl compound, of the following general formula (2), wherein M.sup.1 represents Li or MgZ.sup.1, and Z.sup.1 represents a halogen atom or a (4Z)-4-undecenyl group, subjecting the nucleophilic reagent, (Z)-4-undecenyl compound (2), to an addition reaction with propylene oxide of the following formula (3) to obtain (Z)-7-tetradecen-2-ol of the following formula (4) and oxidizing (Z)-7-tetradecen-2-ol (4) thus obtained to form (Z)-7-tetradecen-2-one (5).

##STR00001##

The present invention relates to a process for preparing (Z)-7-tetradecen-2-one of the following formula (5), the process comprising the steps of converting a (Z)-1-halo-4-undecene compound (1) of the following general formula (1), wherein X.sup.1 represents a halogen atom, into a nucleophilic reagent, (Z)-4-undecenyl compound, of the following general formula (2), wherein M.sup.1 represents Li or MgZ.sup.1, and Z.sup.1 represents a halogen atom or a (4Z)-4-undecenyl group, subjecting the nucleophilic reagent, (Z)-4-undecenyl compound (2), to an addition reaction with propylene oxide of the following formula (3) to obtain (Z)-7-tetradecen-2-ol of the following formula (4) and oxidizing (Z)-7-tetradecen-2-ol (4) thus obtained to form (Z)-7-tetradecen-2-one (5).

##STR00001##

Methods may include obtaining ketones and glycols from a fermentation process, the method including: collecting an off-gas and/or a fermented broth from the fermenter, wherein the off-gas comprises a ketone, and wherein the fermented broth comprises one or more of glycol or ketone; and performing at least one of: transferring the off-gas from the fermenter to a ketone recuperation module; or transferring the fermented broth to a fluid separating module; and isolating one or more of: the ketone from the off-gas; and the glycol from the fermented broth.

Fluorinated fluid conditioning systems are described. In particular, fluorinated fluid conditioning systems including an electrically non-conductive fluorinated fluid and a filter including desensitized activated carbon sorbent are described.

A method for producing astaxanthin incorporates a method for producing astaxanthin-rich algae cells and a method for extracting astaxanthin therefrom. An initial feedstock comprises healthy algae, water, and nutrients. During a growth phase, carbon dioxide and light from a light source are supplied to the feedstock, thereby amplifying the algae. At least a portion of the nutrients remaining after amplification of the algae are separated from the amplified algae. During a stress phase, carbon dioxide and light are supplied to the amplified algae, thereby promoting production of astaxanthin by the amplified algae. The amplified algae and a cover are placed within an interior of an attrition mill having interior surfaces and media which are substantially non-reactive to astaxanthin and milled to release the astaxanthin from the algae. The cover limits oxidation of the released astaxanthin.

Disclosed are methods for dehydrating a water containing source of formaldehyde in which water is separated from the water containing source of formaldehyde using a zeolite membrane. In certain aspects, the water containing source of formaldehyde includes a separation enhancer having a relative static permittivity ranging from 2.5 to 20, and the water containing source of formaldehyde may further include methanol. In certain aspects, (meth)acrylic acid alkyl ester may be produced using the dehydrated source of formaldehyde.