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Scientific Papers Series A. Agronomy

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fertilizers,<br />

outlined<br />

during<br />

thee past<br />

35 years, is<br />

the<br />

expansion<br />

and<br />

diversification of the<br />

range<br />

of<br />

liquid<br />

fertilizers,<br />

regardless<br />

off<br />

the<br />

technologies<br />

of f use<br />

(Cioroianu<br />

ett al.,<br />

2009)<br />

).<br />

The<br />

first “research”<br />

on the posp<br />

ssibility<br />

to use<br />

liquid<br />

fert<br />

tilizerss startedd about<br />

1700 years<br />

agoo<br />

and<br />

coincides<br />

with<br />

the<br />

beginning<br />

of<br />

the<br />

synthesis<br />

of chemical<br />

substancess based<br />

onn<br />

nitrogen<br />

and<br />

ammoniaa (Cioroianu et al., 2009)<br />

).<br />

The<br />

liquid<br />

fertilizers<br />

have<br />

special<br />

advantages<br />

due to thei<br />

ir rapid and<br />

d easy<br />

application, as well<br />

as to<br />

their<br />

higher<br />

agrochemicall efficiencyy as<br />

compared<br />

to<br />

the<br />

clasc<br />

ssical<br />

solidd fert<br />

tilizers<br />

(Cioroianu<br />

et al. , 2009).<br />

elementss wass<br />

obtained.<br />

Under<br />

continuouss<br />

stirring conc<br />

nditions, at a temperature of 25-30 o C, ,<br />

a solution of<br />

microelements (Fe,, Cu,<br />

Zn, Mg, ,<br />

Mn, B) wass chelated withh EDTE<br />

TA disodiumm saltt<br />

andd mixed with a solutionn of potassiumm humatee<br />

(Sîrbu<br />

ett al., 2010)<br />

. The<br />

scheme<br />

to<br />

obtain thee<br />

NPK fertilizers is<br />

presented<br />

in Figure<br />

1.<br />

MATERIALS AND<br />

METHODS<br />

The experimental sch<br />

heme comprised 9 variants<br />

in 4 repetitions:<br />

: V1-<br />

Controll (Non-fertilized);<br />

V2- AH-I<br />

- 100<br />

l/ha;<br />

V3- AH-I - 150<br />

l/ha; V4-<br />

AH-U<br />

- 100<br />

l/ha;<br />

V5- AH-UU - 150<br />

l/ha; V6-<br />

AH-N<br />

- 100<br />

l/ha;<br />

V7- AH-NN - 150<br />

l/ha; V8-<br />

KH<br />

- 100 l/ha; V9-<br />

KHH - 150 l/hal<br />

a.<br />

For the experiment<br />

organizedd onn the slag<br />

g heapp<br />

Figure 1. General sche<br />

emee to obtain<br />

thee NPK fertilizer<br />

for<br />

the corm<br />

crop,<br />

a basic<br />

fertilization was<br />

with humic substances<br />

(accordingg to Pârvan<br />

et al., 2012)<br />

performed<br />

before<br />

sowing, witw<br />

th solid<br />

NPKN<br />

K<br />

15:15:155 - type fertilizers appliedd N – 90 kg/ha,<br />

In<br />

the<br />

framework<br />

of<br />

the<br />

experimentss<br />

P 2 O 5 – 90<br />

kg/ha,<br />

K 2 O - 900 kg/ha,<br />

and<br />

the<br />

performed,<br />

the<br />

potassium<br />

humate<br />

used<br />

too<br />

fertilizer physically<br />

applied<br />

per hectare was<br />

obtain<br />

the fertilizer<br />

was extractedd from<br />

thee coall<br />

600 kg. Before the<br />

sowing,<br />

a basic<br />

fertilizationn<br />

mass,<br />

lignite,<br />

withh the<br />

potassium<br />

carbonatee<br />

was<br />

performed<br />

with<br />

N90PP 90 K 90 and<br />

after<br />

the<br />

solution.<br />

sowing<br />

the<br />

humate-based<br />

liquidd fert<br />

tilizers<br />

Thee potassiumm humate extractedd fromm lignitee<br />

AH-I, AH-U,<br />

of<br />

100-150<br />

l fertilizer/<br />

/ha inn<br />

fertilizerr was thermallyy analyzed in the range<br />

off<br />

450-5000 l of water. The<br />

weedingg operation was<br />

ambient<br />

temperature – 1000°C, inn the<br />

air, withh<br />

performed<br />

60<br />

days<br />

afterr sowing. Soil<br />

samples<br />

a 10 K/mK<br />

inute<br />

heating<br />

rate,<br />

, simultaneouslyy<br />

were<br />

taken<br />

150<br />

days<br />

after<br />

the implementationn<br />

drawing<br />

the<br />

TGA<br />

(thermal<br />

gravimetricc<br />

of<br />

the<br />

experiment,<br />

after<br />

the<br />

first trea<br />

atment<br />

analysis)<br />

), DTG<br />

(derivative<br />

thermogravimetricc<br />

applied<br />

in threee stages,<br />

the<br />

second trea<br />

atment<br />

analysis)<br />

), DTA<br />

(differential thermal analysis)<br />

)<br />

AH-N<br />

andd KH were<br />

applied<br />

in a andd<br />

used<br />

inn<br />

obtaining<br />

the<br />

experimentall<br />

concentration<br />

was applied in three<br />

stages, 2102<br />

0 days<br />

after<br />

the<br />

and<br />

DSC<br />

(calorimetric<br />

analysis)<br />

curves (Sîrbuu<br />

first treatment and<br />

soil samples<br />

were<br />

takenn 600<br />

et<br />

al.,<br />

2010).<br />

The measm<br />

surements were<br />

madee<br />

days<br />

after the<br />

second treatment.<br />

with<br />

a Perkinn Elmerr thermoo balance whichh<br />

The<br />

procedure<br />

to obtain<br />

thee liquid<br />

fertilizer<br />

enabled<br />

mass<br />

determinations at an<br />

error<br />

of<br />

1--<br />

consisted<br />

in<br />

the<br />

neutralizationn<br />

off<br />

the<br />

2%<br />

in thee temperaturee ranr<br />

nge of:<br />

ambientt<br />

phosphoric<br />

acidd con<br />

ncentration<br />

of f 85%<br />

% withh<br />

temperaturee – 1400°CC and<br />

a heating<br />

rate<br />

of: :<br />

potassium<br />

carbonate<br />

concentration<br />

of 98%<br />

%, 0.1-50<br />

K/ /minute.<br />

Thee<br />

potp<br />

tassium<br />

humatee<br />

resulting<br />

in<br />

a solutionn that containedd mono-<br />

place<br />

extraction<br />

from<br />

lignite<br />

presented<br />

four<br />

mainn<br />

under<br />

a<br />

continuous<br />

stirringg at<br />

a constant<br />

decompositionn stages,<br />

namely: up<br />

to 85.3°<br />

°C, ,<br />

andd<br />

obtainedd<br />

in the<br />

laboratoryy<br />

by<br />

alkalinee<br />

dipotassium<br />

phosphate. The<br />

reactionn tookk temperature of 250-300 o C, gradually addingg ann<br />

loss 10.4%,<br />

which stage corresponded to dryingg<br />

amidic,<br />

nitrate and<br />

ammoniumm nitrogen source,<br />

by<br />

an<br />

ende<br />

dothermall process with<br />

a 57.<br />

9 J/gg<br />

and maintainingg the reaction<br />

temperature,<br />

andd<br />

enthalpy; thee secondd<br />

d process<br />

was w<br />

alsoo<br />

as a result<br />

a complexx<br />

mixture<br />

of<br />

macro-<br />

endothermal, in the<br />

e range of o 85.3-267°C,<br />

withh<br />

23

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