INSTALLATION INDUSTRIELLE MOBILE SERVANT A TRANSFORMER EN POUDRE DIFFERENTS LIQUIDES

MOVABLE INDUSTRIAL PLANT TO DRY INTO POWDER DIFFERENT LIQUIDS

Abrégé anglais

ABSTRACT
MOVABLE INDUSTRIAL PLANT TO DRY INTO POWDER DIFFERENT LIQUIDS
One of the ways to carry out this invention can be obtained by
constructing a series of elements properly arranged and assembled.
It is effecient as regards space, function, economy , and
durability that assembled on wheels, following the regulations
required for chassis measures, can achieve what can be done
in an installed plant. This movable industrial plant to dry
into powder several liquids is basically made up of an evaporator,
pulverization drier, boiler, vacuum and centrifugal pumps,
pipes and transport tubes, separators of small particles,
liquid separators, motive power, liquid tanks, electrical system,
etc.
This industrial plant can dry milk into powder, cream, soya bean
milk, fruit juice, soluble coffee, blood, plasma, glands, soap
powder, sewer waste, etc.
This small industrial plant has the advantage of moving to the
place where the raw material is found, which can be dried into
powder at the same time it is produced. Th bacterial and
chemical contamination in the food products is reduced to zero.
Moreover, the organoleptical original characteristics are
preserved. Operative costs are reduced to values that reach
zero. The following is possible: 1) The arrangement and
reappearance of new milking factories in areas very different
from the traditional ones. 2) Due to the low operative costs
the utilization of very important proteins that are normally
lost is possible. For example, blood, plasma, whey, etc.
3) The solution to contamination problems wither chemical or
bacteriological for example drying into powder sewer waste which
later on will have commercial value; drying into powder chemical
substances which are not degradable or are toxic, that otherwise
would contaminate rivers, lakes, seas, etc., at a low cost in
the place of origine and at the same time.

Revendications

CLAIMS
1. Movable industrial plant to dry into powder different
liquids with typical characteristic consisting in an evaporator
(9), a steam condenser (14), a pulverizing drier (30), a boiler
(22), a centrifugal separator of small particles (50), a
centrifugal separator of small particles driven by hot air (32),
a centrifugal separator of small particles driven by cold air
(58). transport ducts, aspiration tubes, aspirator fan (61),
centrifugal pump for liquids (4), vacuum pump (16), cooling
equipment (57'), electric generator, motor, gasoline engines,
power intake, a gasoline tank for engine, a gasoline tank for
boiler, a tank for liquids to dry, with different options in
each stage of the ellaboration in order to adapt to the
characteristics of the liquid to dry. It is capable to dry
into powder liquids with solid particles; installed in a
chassis to be transported to the place where the liquids to be
dried are.
2. A movable industrial plant to dry into powder liquids
according to claims . (1) characterised by having
drying agen distributors, one central (38) and another
peripheral (40), they are adjustable and work synergically
to keep the liquid fractioned in suspension for a longer or
shorter time.
3. An industrial plant to dry into powder liquids according
to claims (1) characterized by an additional vertical
cylinder of turbulence attached to the rotative valves to
unload the powder. Inside the cylinder there helicoidal blades.
4. A movable industrial plant to dry into powder liquids
according to claims (1) with a cooling equipment to
treat powders with fat in their surface.

Description

2 0 ~ ~j rj $ ~
"MQV~LE INDUSTRIAL PLANT TO ~I~Y IN~D POWP~k DIFFE~NT LIQUIDS~'
Thl~ inventl~n mak~s ref~r~nc~ to a s~rles ~f maçhin~s ~nd
elements eh~ are 3ssembled ~n ~ transportable eh~sgls for its
displacem~nt. It~ obJeetivQ Is to dry into powder ~ever~l
subseanc~s . The inv~nt lon cons i stti of ~n evapc~r~tor, ~nç
p~1verlzation drier, motlve pow~r, cen~rlfugat~ sep~r~tor of
sm~l I part ;cles, col lector cyl inder, bol 1~, et~.
The traditional Inethods tha~ nowdal~s w~k successfully, ~re
wel1 known. Thes~ methqds, ~re ~he ones th~t proYlde us
(co~sumers) wlth p~wderod mllkt powderet blood, ~nd plasma~
powdefed eg~s, powdere~ solu~le ~of~e~, powder soap7 powdered
fruit Julce, e~c.
Th~ sy~tem thes~ indu~trie~ L~5e carr~ ths dtfferen~ liq~iTds,
In the b~t p~slble ways, l:o the pl~ce wll~re sp~ctal m~chlnes
~111 transform ~hem in~o powder.
E~Larrlp I e;
To obtnin drl~d rnllk, ~s ~ flrst st~p, w~ havu t~ otloct th~
n~l lk ~rom the farm. Thls i5 d~ne by specl~l trucks whlch tqke
stor ing plants where ;t Is kept until p~steurtz~3tion.
Af~er th~t, it ;s co~led. MlIk is then taken Ir blg speclal
trucks to the dryit~ pl~nes whlch norn~ally pro~ess gr~t
YO I umes .
A simil~r p~oce~s take~ pldc~ with oth~r liquids of easy
decompositTon. Thi~ pro~e~s has an objectlve, i.e. the
preserY~ion of the liqu1d~ in ~he be~t posslble w~y. So that
~fter the ~econstle~tion of ~he mentloned powdor5, the ltquld
would be very slmll~r ~o ~he ortginal llq~td.
Th~ inven~ion h~s th~ pu~po~e of o~taini~g a produ~t of
l~!Xcellellt bacte~101091~1 q~aiTty, ~nd of allow7ng the dav~l~p-
ment of new areas for d~ I ry prodLIc~s ~ c i ~r t G ~7n~s, etc. I t
also h~s ~5 purpo5e, ~h~ uttlizatl~n of was~ed sub~ances
Sinc~ the drylng Into powd~r is a 1;:05tly an~i trout~lesome pr~ces~.
.

~ v3
3~e based on a liq~ld tha~ wlll nut be o~ any use and wlll
then be ev~porated in th~ ~r~ing ylants (~O~O~
,..I'An ~ndustfy on wheel , saVes the rnov~ment of v~hi~10ç ~n
wh~el6 to ~h~t Industry.'l
The ~dv~ntages offered by ~he Inv~ntlon, ar~ malnly ~he
followin~ ones~
In the mTlk indusery, ehe advantage~ are fo~nd in the ~uall~y,
slnce in drying th~ r~cently obtain~d milk ~f ~he cow~ there
is no con~amination, what's mor~, durin~ the procçss prevlous
to the d~ying into powder, tt i5 pas~eurized.
Thls Is s~, becaus~ the transpo~t~ble Industrl~l pl~nt ~o dry
into pQwder dlfferent ~ ids 5~a~t5 to work wi~h the mllklng
of the ~l~st cow ~nd ~nds wlth the milklng of the l~st one,
that 1~ to s~y the mtlk obtalned from th~ cows Is sS~or~d tn
a h~g that conSain~ Sh~ powder obtained d~rTn(J the milking
procèss,
In ~con~rnlc ~rms, the ~dv~llt~ges ar~ ~an~iderable sln~ only
one person cAn take car~ of thtcs ~ovable Indu3try, ~ conventlonal
pick up can tr~snpor~ it, and on rainy days~ ehls c~n be done
by ~nrlord~n~ry eractor. In this way. all th~ op~r~tive expense~
~re reduced to Z~fo.
This ~achine i5 es3sy to 2dapt to the f~t~-hortlcultur~l s;
Industry, be$ause it can be taken to the pla~e where the
plantatlon is loeated, stnce It has sp~ce, motive power,
a citric squeezer and other machines can be applled to It.
A~ss ~h~ ~rasnportabl~ plant has the requl r~d me~sUr~s to
mov~ in the ~i~tes, It can dry Into powder, llquids ~h~t
otherwise wo~ld con~a~inat~ rivers, str~ms and lakes.
These contamln~tln~ liq~id~ ~n b~ ~ran~formed into u~¢f~l
substances ~f c~m~rcial v~lue. For ~xampl~ sewer w~ste,
blood, ~nd slaught~r hou~e ~ste.

. ~ ~
An indust~y of this hlnd, allows dalry exploitatlons"n rre~s
of difficult ~C~ess~ 5in~e ~hls typ~ of ~xplol~ations ~lways
requlre~l a n~rby Industry, ~h;s Is ~lso tru~ Fol othcr
~xplol tat ions~
On~ of the ways to carry ou~ the Inv~ntlon i~ descrlbed In
dotail ~urth~r on. The drawings are only for Ill~stratlon.
Flgur~ N~ 1 i5 ~n explan~tory schen)e o~ on~ of ~he ~t~ferent
ways of Ga rryin~ ~ut thTs tnYention.
Flgu~e ~ 2 ls a Yiew with the purpose of showlng ehe
~rl~ncJemer~ o~ tho whole unle of elements that m~ke up the
transportable industrl21 ptant.
In flCJ~ 1, ma~ked wi~h n~lnb~r 1, ~hlch ind5cae~s the ~ntranc~
c,f the licluid t~ the conatlner ~3) through the -filter ~
th~n through ~h~ pipe (5) wh~re th~ llquld 3~ a~plrated by
th~ centrlf~qal pump (1~, whl~h is op~ra~ed by th~ en~ine (63)
to driv~ ~he llquld thro~h the plp~ t7) that ~nd5 In ~n
~l~m~nt that pulY~rlzo5 upward~, In sm~l I drop~ tilat thon,
wlll ~om~ do~n Up ~o ~ ~ertaln l~vel ('~1) wlthln tho ~v~por~tor
o~ low tempor~ur~5 (~) . Onco thl~ l~v~l has b0en roachcd~
th~ float whlch Is pla~e In th~ tnner part of the evap~ator
(g~ cl~ses the el~ctr~-valve which 1~ p~a~ed ln the ptpe ~5)
and It opens the ~lect~o-valYe whlch 1~ in the plp~ (8),
con~equently, a recyçlirg of th~ llq~llds oc~urs wlthirl the
e.vaporator in a pla~ whlch has temp~ratul^e pr~duced by the
radl~nt (19j. thls radlant 15 reached by all the wa~te~l
gases that ~ome fram the boll~l~ (22) which su~ks ~ir to
produ~e ehe bul~nlng prc~e5s (23~ ~n~l then~ goes ~o the
bur~lel~ (24) through ~he tu~ (17) . This ai r colnes ou~ frorn
the chlnm~y t25) who~ volve (1~ which is piaced in the
~ub~ (17) rey~ tes the te~per~ture. The~n thtlY0 ~J~IS~5 ar~
a~pl rDted by tube t20) whi eh 15 l~aned ta th8 aspl ra~lon
c~ntral ~ub~ t53) to ht! e~pelled to the outside through the
e~h~ust fsn (61) wlllch 15 propelled by ttle Inotor (63),-that
ha t~-mDerheure requi r~ci by the ev~par~t~r (~)

2 ~ 3 ~
! Th~ st~am produc~d in this er1vIronn~nt i5 cond~n~d In laPg~
i radI~tors of large contact surface (14~ ~he abov~ m~ntioned
~dIators (14~ ~hich h~ve ~o co~den~e the steam produ~ by th~
v~c~um p~mp (16~ which is mov~ by th~ mo~or (63) through the
pipes (12~,~13) and (ll) whi~h w;ll drive the vacuum to the
3nsld~ of the evapor~or (~) and thraugh the plpes~ the ~ond~nsed
I . s~e~m ~Ill be expelled. One of ~he 50% Df the ~iquid h~s be~n
evapor~ted (or the rate that ~ per~on ~ishes to ~djust), the
lev~l float (21) will warn the electro~valv~ lo~ated In the
pipe, (6j to sta~ op~ning to gIYe way to the concentrat~ i~to
the 5tOl^ep ~39~ located on the Cop pa~t of ~he pulverizatIon
dr ~ (30),
i This Is ~ither a contInuous or di~contInuou~ process that
i depends on the ed~ustm~nt of the electro-valves hy me~ns of
~he level floa~ whtch is eh~ on~ th~t ~ontrols them at will.
A~ter the con~ trJt~ has bean ob~in~d, we ~ re~dy to ~ork
t wI~h ~h~ pu1vorlz~tlo~ driar (~0) t~ obtaln a gr¢ater y~lld
of the lIquid to be dried.
! PuIverI~tIon drI~r (~0~: It conststs of a biD ~n~ lar~
I dIam~t cyllnd~, tub~ ~r~ arr~n~d In th~ t~p part where the
I drylng agent (hot alr) ent~rs a contain~r in whlch th~ ui~
I to be dried is poured tn ~ ser~cture that ho~ds up ~nd
! operates the rotor, which will pulverl~e ;n small d~ops of
~ I dia~ter.
i These small drop~ ~ill boll ~t susp0nsI~n till the lIquld
1~ consumed In frac~ions o~ sec~nd~ due to the drler ~ger~t
I which makes thern ~t~ee 5~ ~S t~ re~ain the requlred time,
I tlll the whole or p~rtT~I dryTng 1s ~mp1eted. These sm~ll
I drops partlally ~r totally dr~ed will he stores in z cone,
~ue t~ the eff0ct ot' gravit~ ~5 powd~r, snmehow humld
accord7n~ to t~e perlod of expos~r~, th~ ~t~e of ~he drop,
~ the temp~raturo of the drie~ 3~ent, ~ctor~ which ar~ .
: controlled ~t ~111,

2~5~
All that can i~e Elchioved ths~nks to th~ impul~ ~f ~ile en(,~in~
(6~) which di^lY~s ~he pull~y ~ ) whl~ll by ine~n~ ~F hel~s
inci~ea~ the ~pe~d o~ ehe pulley (423, which In turn move3
the rotor (41) W11l~:h Wi i i trans~rin the 1 Iquid that remains
;n tine stor~ (39) intv an homg~neous rain, will~h will be
dr;ed out by th¢ effect of th~ hot alr. Tn~t hot alr
n~e~sary to dry these mlerodrops in ~uspen5ton is pr~viously
heated in the boi ler (22) and thro~gh tubes (35) and (34)
goes to the central distrlbutor ('i8) ~nd to the p~ripheric
distrtbutor (40), ~orrespondin~ to ~he ~I~lves (37) ~nd ~36).
The whoJe air volwne i~ aspirated ~y a tube of big dl~meter
~44) whlch end~ into an aspira~ion intet ~ ; thls hot
~ir loaded wlth humidlty th~t co~es from the drops beln~
evi~porated, is driven by a ~reat ~spiraclon to the centrifufal
s~parator of small parti~les ~50) to ehe stor~, then In ~
c~ntain~r (~2) throu~h a valve ~51) the wet powder that -
in 3 sp~clal c~se ~ would reinain iin s~spension wi~ilin the
~rTer S30).
All of the gas volum~s, ~clqail ~J~ses and w~s~ on~s~ thac
clrculate in ~hIs ~yst~m, ~rc ~splrat~ by ~ie ~xhausit ~an
~61), aa ~n be oi~s~rved In tho dlatJr~in whtch appcar~ In
Flguro Nv 1.
Th~ powder pi~oduced and stored in the pulveriz~tion drier
cone (3~ is ~oll~cted by the rotatiYe valve (4fi) whi~h
pours the p~wder In~o the turbulence ~uct (2~ hen it is
aspir~ted by the pneumatlc duet of transport (31), which
wlll tak~ the powder to the ~entrlf~al Separator oF ~mal
p~rtlçles (32). Thls transport ~itt be c~rrl~ o~t ~ith
c:ool air, or with hot air dependlng on what i~ reqwirad.
A ~econai drylng can bs obt~in~d operatin~ ehe valve ~28): .
whlch is loc~ted In th~ duct (Z7), ehat 1~ at pol,J~er
humldlty Is ad~ustablQ~ ~t wll~, o~herwls~, the environmental
ai r for transport an l)e ~uck~d~
TQ obtain the necess~ry f~rce to ~arry ~u~ this l1e~vy
~ranspor~, the ~pir~tton valYe (47) whl~h is in the tul)}~ ~44)
--5--

- - 2 8 ~ t~
, ~ust b~ closed so ~ to driv~ he aspir~tlon by the
; duct (49) un~il It reaches ~he centrlfugal separator (32)
; ~nd then It passes through the pn~umatic c~nduet (31~.
On~e ~ th~ ve is cl~s~d ~47) ~he ~rier hbS no aspir~t;On
~30).~or thTs re~son ~h~ d~ying process 1~ not per~ormed
during coll~cting timeO All this happens be~use we haYe been
worklng in a lim;ted requlred sp~ee w;th the f~wes~ elements
to achieve an aim. In pr~e~ical eerms every~h7ng is ~ompl~ely
s;mpl~ and easy to perform.
On~ the powder has been obtalned In the centrlfu~al separ~tor
t32) by th~ rbtatiVe valve (54). The powd~r can be p~k~
or le can be stol~ed for i~s subsequsnt pa~klng (59) th~t by
mean~ of the flat v~lve ~6D) i5 ~olle~t~d from ~he centr1f~
s~p2rator ~$~), thls s~c~nd ~eparat~r h3~ ~he p~rti~ul~r7ty of
coollrlg ~he powder at lo~ tcmp~r~ure~, d~le to the cold
produc~d by radlant~ durln~ the a~pl r~ti~n proc~ss t57) th~t
~y mean~ of a c~oling equipnlent produce ~he f~quired low
te~peratures to treat those powders ~hat are fat free on
It~ surfa~.
In Fig~re N~ 1, It 15 possible to see the boller fuel ~anks
~70~; tho~e o~ the engin~ ~6~) and the liquld~ to be prvsessed
t71~. In practical terms~ these ~re located tn the lawe~ P~rt
of th~ ch~s~is floor, that ~s, ~hey are invl~lble ~t firs~
sight, and these tanks, in~rea~e the ~el~h~, lowerin~ the
~en~er of gr~vity, due to 1~5 a~an~e~ent, and Increaslng
the se~bTlity.

Dessin représentatif