The present invention provides an apparatus and methods for producing tetrahydrocannabinolic acid (THCA), cannabichromenic acid (CBCA) and cannabichromenic acid (CBCA) in different ratios. The apparatus comprises: (i) a bioreactor comprising (a) an automated supply system configured to deliver a first automated supply of cannabigerolic acid (CBGA), a cannabinoid acid synthase, and a reaction mixture; and (b) a second automated system to cease the reaction; (ii) a controller configured to modify a property of the reaction mixture to produce the desired products; and (iii) an extractor configured to recover the tetrahydrocannabinolic acid (THCA), cannabichromenic acid (CBCA) or cannabidiolic acid (CBDA) and cannabichromenic acid.

The present invention relates to a process for reacting chemical compounds comprising the step of reacting a compound of formula (IV) ##STR00001##
wherein Hal is independently selected from Cl or Br, and X.sup.? is a monovalent anion, in the presence of an inorganic acid, wherein the aqueous inorganic acid has a concentration of at least about 60%, at a temperature of about 140? C. to about 250? C., to obtain a compound of formula (V) ##STR00002##
wherein Hal is as defined above.

In one aspect, the present disclosure provides methods of preparing a primary or secondary amine and hydroxylated aromatic compounds. In some embodiments, the aromatic compound may be unsubstituted, substituted, or contain one or more heteroatoms within the rings of the aromatic compound. The methods described herein may be carried out without the need for transition metal catalysts or harsh reaction conditions.

In one aspect, the present disclosure provides methods of preparing a primary or secondary amine and hydroxylated aromatic compounds. In some embodiments, the aromatic compound may be unsubstituted, substituted, or contain one or more heteroatoms within the rings of the aromatic compound. The methods described herein may be carried out without the need for transition metal catalysts or harsh reaction conditions.

The present invention provides an apparatus and methods for producing tetrahydrocannabinolic acid (THCA), cannabichromenic acid (CBCA) and cannabichromenic acid (CBCA) in different ratios. The apparatus comprises: (i) a bioreactor comprising (a) an automated supply system configured to deliver a first automated supply of cannabigerolic acid (CBGA), a cannabinoid acid synthase, and a reaction mixture; and (b) a second automated system to cease the reaction; (ii) a controller configured to modify a property of the reaction mixture to produce the desired products; and (iii) an extractor configured to recover the tetrahydrocannabinolic acid (THCA), cannabichromenic acid (CBCA) or cannabidiolic acid (CBDA) and cannabichromenic acid.

The present invention provides an apparatus and methods for producing tetrahydrocannabinolic acid (THCA), cannabichromenic acid (CBCA) and cannabichromenic acid (CBCA) in different ratios. The apparatus comprises: (i) a bioreactor comprising (a) an automated supply system configured to deliver a first automated supply of cannabigerolic acid (CBGA), a cannabinoid acid synthase, and a reaction mixture; and (b) a second automated system to cease the reaction; (ii) a controller configured to modify a property of the reaction mixture to produce the desired products; and (iii) an extractor configured to recover the tetrahydrocannabinolic acid (THCA), cannabichromenic acid (CBCA) or cannabidiolic acid (CBDA) and cannabichromenic acid.

The present invention provides an apparatus and methods for producing tetrahydrocannabinolic acid (THCA), cannabichromenic acid (CBCA) and cannabichromenic acid (CBCA) in different ratios. The apparatus comprises: (i) a bioreactor comprising (a) an automated supply system configured to deliver a first automated supply of cannabigerolic acid (CBGA), a cannabinoid acid synthase, and a reaction mixture; and (b) a second automated system to cease the reaction; (ii) a controller configured to modify a property of the reaction mixture to produce the desired products; and (iii) an extractor configured to recover the tetrahydrocannabinolic acid (THCA), cannabichromenic acid (CBCA) or cannabidiolic acid (CBDA) and cannabichromenic acid.

The present invention provides an apparatus and methods for producing tetrahydrocannabinolic acid (THCA), cannabichromenic acid (CBCA) and cannabichromenic acid (CBCA) in different ratios. The apparatus comprises: (i) a bioreactor comprising (a) an automated supply system configured to deliver a first automated supply of cannabigerolic acid (CBGA), a cannabinoid acid synthase, and a reaction mixture; and (b) a second automated system to cease the reaction; (ii) a controller configured to modify a property of the reaction mixture to produce the desired products; and (iii) an extractor configured to recover the tetrahydrocannabinolic acid (THCA), cannabichromenic acid (CBCA) or cannabidiolic acid (CBDA) and cannabichromenic acid.

The present invention provides an apparatus and methods for producing tetrahydrocannabinolic acid (THCA), cannabichromenic acid (CBCA) and cannabichromenic acid (CBCA) in different ratios. The apparatus comprises: (i) a bioreactor comprising (a) an automated supply system configured to deliver a first automated supply of cannabigerolic acid (CBGA), a cannabinoid acid synthase, and a reaction mixture; and (b) a second automated system to cease the reaction; (ii) a controller configured to modify a property of the reaction mixture to produce the desired products; and (iii) an extractor configured to recover the tetrahydrocannabinolic acid (THCA), cannabichromenic acid (CBCA) or cannabidiolic acid (CBDA) and cannabichromenic acid.

A process for the manufacture of a terphenyl compound [compound (T), herein after] of formula (T): wherein each of R and R, equal to or different from each other, are selected from the group consisting of halogen, alkyl, aryl, ether, thioether, ester, amide, imide, alkali or alkaline earth metal sulfonate, alkyl sulfonate, alkali or alkaline earth metal phosphonate, alkyl phosphonate, amine and quaternary ammonium; each of j and k, equal to or different from each other, are zero or are an integer from 1 to 4, including the steps of (i) reacting at least one organozinc compound of formula (I) with at least one dihalocompound of formula (II) in the presence of a catalyst compound; wherein Y is selected from the group consisting of a chloride, a bromide, an iodide, an alkanesulfonate or a fluoroalkanesulfonate anion, R2 is selected from selected from the group consisting of C.sub.1-C.sub.10-alkyl, C.sub.3-C.sub.10-cycloalkyl, C.sub.1-C.sub.10-halooalkyl and C.sub.3-C.sub.10 halocyclo alkyl, each of Z, equal to or different from each other, are selected from the group consisting of a chloride, a bromide, an iodide, an alkanesulfonate or a fluoroalkanesulfonate anion; (ii) a Bayer-Villiger oxidation and (iii) hydrolysis or alcoholysis.

##STR00001##