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Apparatuses and methods are described for parallel oligonucleotide synthesis of hundreds of different sequences and lengths at a time. Standard phosphoramidite chemistry is employed. The syntheses take place in a reaction plate compatible with the industrial standard microplate format to allow the u

Apparatuses and methods are described for parallel oligonucleotide synthesis of hundreds of different sequences and lengths at a time. Standard phosphoramidite chemistry is employed. The syntheses take place in a reaction plate compatible with the industrial standard microplate format to allow the use of readily available automated instruments for subsequent processing. Key parameters in reducing synthesis volume in small reaction wells are discussed. This invention provides solutions to the difficulties of low volume, high number synthetic reactions.

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1. A method of conducting parallel chemical synthesis comprising:determining an optimal ejection velocity for dispensing a plurality of fluids through a supply assembly into reaction wells of a synthesis apparatus by measuring a set of coefficients of variation and a set of synthesis support spatter

1. A method of conducting parallel chemical synthesis comprising:determining an optimal ejection velocity for dispensing a plurality of fluids through a supply assembly into reaction wells of a synthesis apparatus by measuring a set of coefficients of variation and a set of synthesis support spattering heights for each of the fluids as a function of ejection pressure to derive an optimal ejection pressure at which both reagent accumulation and synthesis support spattering height are minimized for dispensing the fluids wherein a maximal optimal ejection pressure applicable for all of the fluids defines the optimal ejection velocity for dispensing each individual fluid, dispersing the fluids via the supply assembly at the determined optimal ejection velocity into the reaction wells of a synthesis apparatus, and reacting the fluids within the reaction wells. 2. The method of claim 1, wherein the reaction wells each have a synthesis reaction medium which includes a synthesis support disposed on a membrane through which reagents are drained with a gas flow rate lower than a pumping rate, where the gas flow rate is the rate at which an inert gas passes through the reaction wells and the pumping rate is the rate at which a pumping assembly of the synthesis apparatus operates.3. The method of claim 2, wherein the dispensed fluids are reactants, said synthesis apparatus is a parallel synthesis plate, and each of the wells is defined by a bore extending from a first end to a second end of each well, includes the synthesis reaction medium disposed within the well between the first and second ends, and has an opening at the first end having an inner diameter of about 3.5 mm or less, an inner diameter at the synthesis reaction medium closest to the second end of about 3.0 mm or less, and each of the wells are arranged i a z-dimensional array such that the wells are spaced apart from neighboring wells center-to-center by about 4.5 mm or less; and the supply assembly includes at least one valve for dispensing fluids through a nozzle, the valve and nozzle together configured to provide fluids to wells in volumes as small as about 2 microliters.4. The method of claim 3, wherein the nozzle is made from a material having a surface energy of about 20dynes/cm or less and has a de-burred tip.5. The method of claim 3, wherein the synthesis is carried out on synthesis supports retained by a porous membrane.6. The method of claim 5, wherein the membrane has a bubble point pressure above 10 in. Hg, the bubble point pressure being a differential gas pressure at which the first steady stream of gas bubbles are emitted from the membrane when immersed in a liquid.7. The method of claim 5, further comprising draining each of the wells via a pumping assembly, wherein the pumping assembly is in communication at the second end of the wells for applying a vacuum thereto, and the membrane has a bubble point pressure higher than the applied vacuum, the bubble point pressure being a differential gas pressure at which the first steady stream of gas bubbles are emitted from the membrane when immersed in a liquid.8. The method of claim 1 further comprising performing chemical synthesis in the wells on a reaction scale of less than about 20 nanomole.9. The method of claim 8 further comprising performing chemical synthesis in the wells on a reaction scale of less than about 10 nanomole.10. The method of claim 9 further comprising performing chemical synthesis in the wells on a reaction scale of less than about 5 nanomole.11. The method of claim 3 further comprising performing chemical synthesis in parallel in more than about 100 wells.12. The method of claim 11 further comprising performing chemical synthesis in parallel in more than about 300 wells.13. The method of claim 12 further comprising performing chemical synthesis in parallel in more than about 1,000 wells.