Worm Breeder's Gazette 8(2): 56

These abstracts should not be cited in bibliographies. Material contained herein should be treated as personal communication and should be cited as such only with the consent of the author.

Buckets of Worms

A.O.W. Stretton, C.D. Johnson, P. Anderson

In order to provide sufficient material for partial purification of 
minor nematode proteins preliminary to immunization and selection of 
monoclonal antibodies, we have developed a method for growing C.  
elegans (sometimes referred to as 'the nematode') in the 300 liter 
fermenter located in the Department of Biochemistry.  Briefly, a 250 
liter bacterial culture was grown in the fermenter and collected with 
a continuous flow centrifuge.  Two kilograms of the bacteria were 
resuspended in 250 liter of S medium in the fermenter and seeded with 
10 nearly exhausted 1 liter shaker cultures of C.  elegans.  With 
stirring and vigorous aeration, the worms grew rapidly and appeared 
very healthy.  After 4 days, as the bacterial count began to decline, 
we added the remainder (3 kilograms) of the bacterial pellet.  We 
harvested the worms, by continuous flow centrifugation on day 6.  
Worms were resuspended in ice cold water and recentrifuged.  The 
pellet was resuspended in cold 35% sucrose and the worms collected by 
flotation.  After washing twice with water, the final pellet (1.35 
kilograms) was resuspended in a small amount of water, dripped into 
liquid nitrogen and the nuggets (which resemble garbanzo beans, but 
taste like chicken) stored at -80 C.
Specific 
Notes:
1)  Bacterial Growth Medium: A less expensive modification of 3XD 
was used.  This medium, developed by Paul Gardner and Dick Russell, 
which we call GaRuM, contains per liter 10.5gm Na2HP04, 4.5gm KH2P04, 
3.0gm NH4Cl, 25gm Sigma #C0626 Casein hydrolysate, 25ml glycerol, 0.
1gm uracil and 0.2gm streptomycin sulfate.  After autoclaving, 4ml 1M 
MgS04 and 1.0ml trace metals (1.0mM FeS04, 1mM MnS04, 0.5mM ZnS04, 0.
5mM CuS04, 4 M Na2MoO4, 0.1M KCl, 0.1M NaCl) were added.  Sterile 
antifoam was added automatically throughout the growth to control 
excess foaming.
2)  E.  coli strain OP50-1: A variant of OP50, the standard uracil 
requiring strain, was selected to be resistant to phage phi80 (and 
therefore cross resistant to phage T1).  Phage-resistant OP5O was 
further selected to be resistant to streptomycin using mutagenesis 
with nitrosoguanidine.  We call the phi80 and streptomycin resistant 
strain OP50-1.  We now use OP50-1 routinely in combination with 
streptomycin and mycostatin in both liquid cultures and in agar.  
Contamination problems are greatly reduced.
3)  Nematode Growth Medium: S medium with 0.2gm/liter streptomycin 
and 50,000 units/liter mycostatin.  The mycostatin was suspended in 
70% ethanol and added after autoclaving.
4)  Harvesting: Bacteria were collected with a Sharples centrifuge 
at 3 liters/minute.  Prior to use, the centrifuge bowl was autoclaved 
and the tubing from the fermenter to centrifuge steam sterilized.  
Bacteria were scraped into sterile beakers and stored at 4 C.  
Nematodes were harvested at 15 liters/minute.  One ml samples were 
monitored at ~2minute intervals during the harvest; no worms were 
observed in any sample.
5)  Ciliate Contamination: On day 4 after initiation of the nematode 
culture, we noticed the presence of small ciliates (possibly the 
species Colpoda claimed to have air-borne, autoclave-resistant spores).
The ciliates grew rapidly and threatened to overgrow the culture.  
After investigating several possible treatments, we found that a 
1/1500 dilution of commercial bleach selectively eliminated the 
ciliates with no apparent effect on the worms.  The final product 
contained no trace of ciliates.
6)  Yield: We harvested the nematodes well before exhaustion of the 
bacteria in order to obtain healthy well-fed worms since starved worms 
have lower levels of choline acetyltransferase (one of the enzymes to 
which we are attempting to generate monoclonal antibodies).  Yield 
would have been substantially larger if grown to exhaustion.
7) Cost: Approximately $200 for media and $265 for use of the 
fermenter.