CA1224374A

CA1224374A - Soil releasing detergent

Info

Publication number: CA1224374A
Application number: CA000450756A
Authority: CA
Inventors: Robert J. Steltenkamp; Loretta K. Ciallella; Michael A. Collins
Original assignee: Colgate Palmolive Co
Current assignee: Colgate Palmolive Co
Priority date: 1983-03-29
Filing date: 1984-03-28
Publication date: 1987-07-21
Also published as: FR2543568B1; PH23380A; NO161981C; NO841229L; GB8407970D0; FR2543568A1; IT8447941A1; IT8447941A0; ES8603559A1; PT78333B; CH660198A5; NL8400996A; FI841243A7; AT395164B; NZ207536A; SE459972B; ZW4784A1; AU563631B2; DE3410810A1; FI76117B

Abstract

ABSTRACT OF THE DISCLOSURE

A particulate built nonionic synthetic organic de-tergent composition, useful for washing synthetic organic poly-meric fibrous materials, such as polyesters and polyester-cotton blends, and imparting soil release properties to them, includes nonionic synthetic organic detergent, alkaline builder or mixture of builders for such detergent, a soil releasing co-polymer of polyethylene terephthalate and polyoxyethylene tere-phthalate, and polyvinyl pyrrolidone (PVP). The PVP and the soil releasing polymer may be applied to base beads of builder salt(s) as a spray, in nonionic detergent. Alternatively, the PVP may be present as a coating on particles of the soil releas-ing polymer, which are blended with base builder beads onto which liquid state nonionic detergent has previously been sprayed and in which such spray has been absorbed. Such presence of PVP
increases the soil releasing capability of the composition after storage.

Description

3~
This invention re]ates to detergent compositions which are useful for washin~ synthetic organic polymeric fibrous materials, such as polyesters, and which impart soil releasing properties to such washed materials. More particu-larly, the invention relates to such compositions in parti-culate form which contain as the soil releasing agen-t therein a copolymer of polyethylene terephthalate and polyoxyet'nylene terephthalate, a nonionic detergent, an alkaline builder which can decrease the soil releasing effectiveness of the soil releasing material when in contact wi-th such material during storage, and a stabilizing proportion of polyvinyl pyrrolidone (PVP) to help to maintain the soil releasiny characteristics of the soil releasing copolymer despite the presence of the alkaline builder.
In our Canadian Patent Application Serial ~o. 432,116 there are described built nonionic synthetic organic detergent compositions which contain a preferred type of soil releasing copolymer of polyethylene terephthala-te and polyoxyethylene terephthalate. When polyester or polyes-ter-cotton blend fabrics and items made From such fabrics have been washed in the described products such fabrics acquire soil releasing proper-ties so that when -they are subsequently soiled with a lipophilic material, such as dirty motor oil, such soil can more readily be removed during washing of the fabric, whether such washing is with the invented detergent composition or with a conventional Laundry detergent product. It has been proposed to dissolve the mentioned type of soil releasing poly-mer of polyethylene terephthalate and polyoxyethylene tereph-thalate in molten nonionic detergent and to spray the solution onto absorbent spray dried beads of builder material. The described compositions and the me-thod for -the manufacture thereof are useful but in some cases, as when the builder is alkaline, its presence can adversely affect the soil releasing capability of the soil releasing polymer in the mentioned detergent compositions, after storage at room temperatures and especially after storage at elevated temperatures. This appears to be due to the sensitivity of the soil release pro-moting polymer to hydrolysis. It has now been discovered that when PVP, preferably of a certain type (molecular weight range), is present in the detergent composi-tion in intimate contact with the soil releasing polymer, sometimes coating it, the soil releasing capabili-ty of the detergent composition containing such polymer is significantly improved after stor-age, compared to a similar product in which no PVP is present.
In accordance with the present invention a particu-late built nonionic synthetic organic de-tergent composition for washing synthetic organic polymeric fibrous materials and im-parting soil release properties to them comprises a detersive proportion of a nonionic synthetic organic detergent~

a bullding proportion of a water soluble alkaline builder for such detergent, a soil releasing proportion of a soil releasing polymer of polyethylene terephthalate and polyoxyethylene tere~
phthalate, and a stabilizing proportion of polyvinyl pyrrolidone (PVP) for stabilizing the soil releasing polymer in the presence of the alkaline builder. In another aspect, the present inven-tion provides a process for manufacturing a particulate built nonionic synthetic organic detergent composition for washing syn-thetic organic polymeric fibrous materials and imparting soil re-lease properties to them, which composition includes a detersiveproportion of a nonionic synthetic organic detergent, a building proportion of a water soluble alkaline builder for such detergent, a soil releasing proportion of a soil releasing polymer of poly-ethylene terephthalate and polyoxyethylene terephthalate, and a stabilizing proportion of PVP for stabilizing the soil releasing polymer in the presence of the alkaline builder, which comprises spray drying an aqueous crutcher mix of the alkaline builder to produce dried particles thereof, and applying to such spray dried builder particles either (i) the nonionic detergent in liquid state containing the soil releasing polymer and the PVP, so that the nonionic detergent, soil releasing polymer and PVP
are absorbed by the spray dried builder particles, or (ii) the nonionic detergent in liquid state so that it is absorbed by the spray dried builder particles, applying PVP in a liquid medium to particles of the soil releasing polymer and mixing such re-sulting particles with the builder particles containing nonionic detergent.
Preferably the water soluble alkaline builder salt will be sodium tripolyphosphate (normally pentasodium tripolyphosphate), which may be accompanied by sodium silicate, a certain type of polymer of polyethylene -terephthala-te and polyoxyethylene tere-phthalate will be used, the nonionic detergen-t will be a con-densation product of higher fatty alcohol and ethylene oxide, and the PVP will be water soluble and within a given molecular weight range. Limited proportions of moisture and adjuvants may also be present in the invented compositions. Also within the invention are processes for the manufacture of the described stabilized soil releasing detergent compositions, and methods for washing materials with such compositions.
Although various nonionic de-tergents of satisfactory physical characteristics may be utilized, including condensa-tion products of ethylene oxide and propylene oxide with each other and with hydroxyl-containing bases, such as nonyl phenol and Oxo-type alcohols, for best results it is highly preferred that the nonionic detergent be a condensation product of ethylene oxide and higher fatty alcohol. In such - 4a -3~

products the higher fatty alcohol is of 10 to 20 carbon atoms, preferably 12 to 15 or 16 carbon atoms, and the nonionic detergent con ains from about ~ ~o 20 or 30 ethylene oxide groups per mole, preferably from 6 to 11 or 12. Most preferably, the nonionic detergent will be one in which the higher fatty alcohol is of about 12 to 15 or 12 to~14 carbon atoms and which contains from 6 or 7 to 11 moles of ethylene oxide. Among such detergents is Alfonic~l2l4-6oc~ sold by the Conoco Division of ~.I. DuPont de Nemours, Inc., and Neodols 23-6.5 and ~5-7, available from 5hell Chemical Company. Among their especially attractive properties, in addition to good detergency with respect ~o oily and greasy soil deposits on goods to be washed, and excellent compatibi-lity with the present polymeric release agents, is a compara-tively low melting point, which is still appreciably above room temperature, so that they may be sprayed onto base beads as a liquid which solidifies quickly after it has penetrated into the beads (m.p. usually being in 40 to 55C. ran~e).
Various builders and combinations thereof which are effective to complement the washing action of the nonionic synthetic organic detergent(s~ and to improve such action include both water soluble and water insoluble builders. Of the water soluble builders, which preferably are employed in this invention, and are preferably in mixture, both inorganic and organic builders may be useful. Among the preferred 3~

inorganic water soluble builders those that are best include :
various phosphates, preferably polyphosphates, such as the tripolyphosphates and pyrophosphates, more specifically the sodium tripolyphosphates and sodium pyrophosphates, e.g., pentasodium tripolyphosphate, tetrasodium pyrophoSphate;
sodium carbonate, preferably as soda ash; and sodium silicate;
and mixtures thereof. The sodium silicate is normally of Na2O:SiO2 ratio within the range of 1:1.6 to 1:3, preferably 1:2.0 to 1:2.4 or 1:2.8, e.g., 1:2.4. Of the water soluble inorganic builder salts the phosphates will usually be employed in greater proportion, with a lesser proportion of sodium silicate, the carbonate may be employed with bicarbonate and often with a lesser proportion of sodium silicate, and the silicate will rarely be used alone. Instead of individual polyphosphates being utilized it will sometimes be preferred to employ mixtures of sodium pyrophosphate and sodium tripoly-phosphate in proportions within the range of 1:10 to 10:1, preferably 1:5 to 5:1. Of couxse, it is recognized that changes in phosphate chemical structure may occur during crutching and spray drying, so that the final product may differ somewhat from the components charged to the crutcher.
It will be noted that the water soluble builders mentioned are alkaline materials and usually the alkalinity resulting will be such that a 1~ aqueous solution of the detergent composition will be of a pH in the range of about 3~

8.5 to 12, e.g., 10Ø This alkalinity helps the detergent composition to remove various types of soil from laundry and to hold it in suspension but it also has a negative effect, tend.ing to cause degrada~ion of the soil releasing polymer S employed and thus interfering with such polymer i~par~ing 50il releasing properties to washed materials.
Because polyesters, whe~her employed alone or in blends with cotton, are lipophilic, they tend to attract and hold lipophilic soils, which consequently may still be present on laundry after washing, rinsing and drying.
Therefore, especially with respect to polyester fihers, the imparting of soil release properties to the fibers of materials being washed is important so that the laundering thereof may be effective. Consequently, especially because in recent years many articles of clothing and o~her washable household goods have been made from polyesters or polyester blends it is important that maximum soil release properties be imparted to such material. Therefore, any tendency of the soil releasing polymer being employed to degrade should be counteracted. Thus, the discovery that a certain material (PVP) s~abilizes the soil releasing polymer employed in this invention is an important one.
The soil release promoting polymer which is an essential component of the compositions of this invention is a polymer of polyethylene terephthalate and polyoxyethylene terephthalate which is dispersible in water and is depositable 3'7~

from wash water containing nonionic detergent and builder for the nonionic detergent, onto synthetic organic polymeric fibrous materials, especially polyesters and polyester blends, so as to impart soil release properties to them, while maintaining them comfortable to a wearer of clothin~
made from such materials and not preventing or significantly inhibiting vapor transmission throuyh such clothing. Such polyesters have also been found to posses~ anti-redeposition properties and often assist in removing stains from substrates.
They tend to maintain soil, especially oily or greasy soil, dispersed in wash water during washing and rinsing, so that it is not redeposited on the laundry. Useful such products are copolymers of ethylene glycol or other suitable source of ethylene oxide moiety, polyoxyethylene glycol and tere-phthalic acid or suitable source of the terephthalic moiety.The copolymers may also be considered to be condensation products of polyethylene terephthalate, which may sometimes be xeferred to as an ethylene terephthalate polymer, and polyoxyethylene terephthalate. While the terephthalic moiety is preferred as the sole dibasic acid moiety in the polymer it is within the invention to utilize relatively ~mall proportions of isophthalic acid and/or orthophthalic acid (and sometimes other dibasic acids, too) to modify the properties of the polymer. However, the proportions of such acids or sources of such supplemental moieties charged to the reaction mix, and the corresponding proportions in the ~2~3~7~

final polymer will normally be less than 10% each of the total phthalic moieties present, and preferably will be less than 5% thereof.
The molecular weight of the polymer will be in the range of about 15,000 to 50,000, preferably being about 19,000 to 43,000, more preferably being about l9,000 to 25,000, e.g., about 22,000. Such molecular weights are weight average molecular weights, as distinguished from number average molecular weights, which, in the case of the - 10 present polymers, are often lower. In the polymexs utilized the polyoxyethylene will be of a molecular weight in the range of about 1,000 to 10,000, preferably about 2,500 to 5,000, more preferably 3,000 to 4,000, e.g., about 3,400.
In such polymers the molar ratio of polyethylene terephthalate to polyoxyethylene terephthalate units (considering OCH2CH2O-C- ~ -C3 and ~(OCH2CH2)n-O-C- ~ -C~

as such units) will be within the range of 2:1 to 6:1, highly preferably 5:2 to 5:1, even more preferably 3:1 to 4:1, e.g., about 3:1. The proportion of ethylene oxide to phthalic moiety in the polymer will be at least 10:1 and often will be 20:1 or more, preferably being within the range of 20:1 to 30:1 and more preferably being about 22:1.
Thus, it is seen that the polymer may be considered as being essentially a modified ethylene oxide polymer, with the phthalic moiety being only a minor component thereof, 3~

whether calculated on a molar or weight basis. It is considered surprising that with such a small proportion of ethylene terephthalate or polyethylene terephthalate in the polymer the polymer is sufficiently similar to the polymer of the polyester fiber substrate (or other polymers to w~ich it is adherent, such as polyamides) as to be retained thexeon during the washing, rinsing and drying operations. Yet, as shown by comparative experiments and various washing tests in which soil release is measured, the described polymer, in the present detergent compositions, is effecti~e to deposit on washed synthetics, especially polyesters, so as to make them better able to be washed free of oily soil by a built nonionic detergent composition or other detergent product.
It is considered that the polymer's increased hydrophilicity, attributable to the large proportion of hydrophilic ethylene oxide moieties therein, may be responsible for the excellent soil release properties which it imparts to the material upon which it is deposited, and such may also help it to coact with the built nonionic detergent.
Various li~erature articles, texts and patents disclose methods for the manufacture of the present polymers, included among which are Journal of Polymex Science, Vol. 3 pages 609-630 (1948); Journal of Polymer Science, Vol. 8, pages 1-22 (1951); Fibers ~rom Syn~hetic Polymers, by Bill, published by Elsevier Publishing Company, New York, New Yor~
(19~3), at pages 320-322; British patents 1,088,984 and ~2~ 7~L
1,119,367; and U.S. patents 3,557,039; 3,893,929; and 3,959,230. Although suitable methods for making the instant polymers are described in such references it is considered that none of them discloses the particular polymers which are utilized in the present invention (but some such are available commercially) and none discloses the present detergent composi-tions. Such polymers may be considered as having been randomly constructed from polyethylene terephthalate and polyoxyethylene terephthalate moieties, such as may be obtained by reacting polyethylene terephthalate (e.g., spinning grade) and polyoxy-ethylene terephthalate or reacting the ethylene glycol, poly-o~yethylene glycol and acid ~or methyl ester) precursors there-of. Yet, it is also within the invention to utilize more ordered copolymers, such as those made by reacting components of predetermined or known chain lengths or molecular weights, so as to produce what might be referred to as block copolymers or non-random copolymers. Graf-t polymers may also be practic-able.
The described materials are available from various sources, the products of one of which will be described in more detail here. Useful copolymers for the manufacture of the detergent compositions of this invention are marketed by Alkaril Chemicals, Inc., and commercial products of such company that have been successfully employed to produce , ~
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~J~3~4 satisfactory soil release promoting detersent compositions are those sold by them under the trademaxks Alkaril QCJ ~nd Alkaril QCF, formerly Quaker QCJ and Quaker QCF. Products available from them in limited quantities, designated by them as 2056-34B and 2056-41, have also been found to be acceptable. The QCJ pxoduct, normally supplied as an aqueous dispersion, is also available as an essentially dry solid (QCF).
When it is anhydrous or low in moisture content (preferably less than 2% moisture), it looks like a lisht brown wax, and in it the molar ratio of ethylene oxide to phthalic moiety is about 22:1. In a 16% dispersion in water the viscosity at 100C., is about 96 centistokes. The 2056-41 polymer is like a hard, light brown wax and in it the hydrophile:
hydrophobe ratio is about 16 to 1, with the viscosity being about 265 centistokes. The 2056-34B polymer appears to be a hard brown wax, with a hydrophile.hydrophobe ratio of about 10.9:1 and its viscosity, under the same conditions as previously mentioned, is about 255 centistokes. The higher the molecular weight of the polymer the lowex ~he hydrophile:
hydrophobe molar ratio may be therein and still result in satisfactory soil release promotion by the invented detergent compositions. The QCJ and QCF polymers have melting points ~by differential thermal analysis) of about 50 to 60~C.(but minor proportions of such products will remain ln solid state at temperatures up to 100C.),a carboxyl analysis of 5 to 30 equivalents/106 grams and a pH of 6 to 8 in distilled water at 5~ concentration. The molecular weights (weight average) are in the range of 20,000 to 25,000 and the ethylene tere-phthalate:polyoxyethylene terephthalate units molar ratio is d ~: 3~7~

about 74:26. All three of the mentioned trademarked products are water soluble or substantially water soluble in warm or hot water ~at 40 to 70C.) or at least are readily dispersible, and may be characterized as of high molecular weight, over 5 15,000, generally in the range o 19,000 to 43,000, often pre-ferably 19,000 to 25,000, e.g., about 22,000. In the present application when proportions of the soil release polymer are given such are on the basis of the polymer, including any in-solubles therein (which can be less active as soil release agents). Ideally, the release polymer employed will be 100%
water soluble.
Normally, for "~olution" application to materials or for solution addition to a detergent composition in wash water, the copolymers of this invention may be employed in aqueous dispersion. In such dispersions a surface active agent may be present to assist in maintaining the dispersion uniform. Only small proportions of such surface active agent will be employed, if any. Normally, the concentration of the polymer in the aqueous medium will be about 5 to 25%, on a composition basis, preferably 10 to 20%, e.g., 16%, and such is the concentration at which the mentioned commercial products are normally supplied when a liquid form is desired.
While li~uid dispersions or solvent solutions of the polymer may be employed for direct additions of the pol~mer to the medium in which the fabrics are to be treated, when the polymer is to be incorporated in a particulate detergent composition it will be preferable for it to be in solid form, preferably as an anhydrous particulate solid of a particle size like that of the other detergent composition components. Alternatively, it may be finely divided and powdered onto spray dried beads of the other components. In more pref~rred methcds of incorporation in a detergent composition the polymer may be dissolved in nonionic detergent and sprayed onto base beads or may ~e prilled with-carriers and mixed with the base beads. It has been found that the polvmer should not be added to an aqueous crutcher mix containing anionic detergent and/or builder salt and it should not be brought into contact with water soluble - 10 builder salt in the presence of moisture, especially at an elevated temperature. Accordingly, to make free flowing particulate product, normally the polymer will be essentially dry or very low in moisture content. The use of such a product also allows for the manufacture of base beads at normal moisture content without the moisture content thereof being increased objectionably by post-spraying of an aqueous dispersion of the polymer onto the beads.
The PVP employed has been found effective in stabilizing the described soil releasing polymers in the presence of alkaline builder, and is especially effective in the presence of sodium tripolyphosphate, which may be accompanied by sodium silicate. Such PVP usually has a molecular weight in the range of about 5,000 to 200,000, preferably 10,000 to 160,000 and most preferably about 10,000 to 50~000O However, in some cases PVP with a molecular weight greater than '7~

200,000 has been found useful, although not as effective as the compounds within the ranges given. Thus, PVP with a molecular weight of about 360,000 exhibits some stabilizing effect but normally will be uneconomic in view o~ the superior results obtained with the lower molecular weight products.
A preferred source of PVP i5 GAF Corporation, New York, N.Y., ana the preferred commercial products of that company are marketed under the designations K-15 (M.W. = lO,000), K-30 (M.W. = 40,000) and K-60 (M.W. - 160,000)~ Their K-90 product : 10 has a molecular weight of about 360,000. All the described products are water ~oluble and additionally, are soluble in molten nonionic de~ergent of the type preferably employed in accordance with this invention (a condensation product of a higher fatty alcohol with ethylene oxide). While PVP is highly preferred it is considered that other polylactams, such as polyvinyl oxazolidinone, may also be useful in at least partial replacement of the PVP. Polyacrylamide and related amides possess some stabilizing properties too, but they are inferior to PVP in this respect.
Various suitable adjuvants may be present in the invented detergent compositions, such as enzyme powder, which helps to decompose stains and other soils so as to promote their removal, ~hereby coacting with the soil release aiding polymer;
perfumes; fluorescent brighteners; colorants (dyes and water dispersible pigments, such as ultramarine blue3; bactericides;
fungicides; and flow promoting agents. Some of these materials may be added in the crutcher so that they are parts of the base beads, and some of them will be pos~-added. Inorganic fillers, such as sodium sulfate and sodium chloride, may be utilized but prefera~ly the proportions thereof will be limited, one reason for this being because it has been found that sodium sulfate tends to react adversely with the present polymers. Of the enzymes, both prsteolytic and amylolytic enzymes may be employed, such as those sold under the tradenames Alcalase, manufactured by Novo Industri, A/S, and Maxazyme, both of which are alkaline proteases (subtilisin).
In the invented detergent compositions the proportion of synthetic organic nonionic detergent will be from about 5 to 30%, preferably 10 to 25% and more preferably 15 or 18 to 22%, e.g., about 20 or 21%. The to~al proportion of water soluble alkaline builder will be from about 30 to 80%, preferably from 40 to 75%, and more preferably 45 to 70~.
When the builders are sodium tripolyphosphate and sodium silicate, as is preferred, the proportions thereof are preferably about 30 to 70% and 3 to 15%, respectively, more preferably 40 to 65% and 5 to 13%, e.g., 54% and 10%. The proportion of soil release promoting polymer will be from about 0.5 to 20%, preferably 1 to 10%, more preferably 1 to 5~ and most preferably 2 to 5%, e.g., 3%. The moisture content of the product will usually be from 1 to 20%, preferably 3 to 15% and more preferably 5 to 12%, e.g., 9%.
Individual adjuvants preferably constitute no more than 10~
of the composition, more preferably being limited to 5% and often to 2 or 3%, with the total of adjuvants desirably not exceeding 25%, preferably being limited to 1~% and more preferably being held ~o 5 or 10~ of the composition. Of course, mixtures of individual components of the invented compositions and of adjuvants for them may often be desirably employed, and such are intended to be included when a single type of component is mentioned. Enzyme powder, when present, will usually be at a concentration in the range of 0.5 to 3~, preferably 1 to 2~. Such enzyme powder is commercially available as a mixture of active enzyme and carrier material, e.g., Maxazyme 375.
The detergent composi~ions, whether previously manufactured and stored before use, or made immediately prior to use, may be employed in dilute aqueous solution (or dispersion) in wash water to wash all~synthetic mate~ials, including polyesters; cotton-synthetic blends, including cotton-polyester blends; cotton~; nylons; and mixtures of such materials. Normally the dry weight of materials being washed will be from 2 to 15 or 20~ of the weight of the aqueous washing medium, and preferably S to 10% thereof.
The wash will be conducted with agitation over a period from 5 minutes to 1/2 hour or one hour, often from 10 to 20 minutes, and after washing the materials will be rinsed, usually with several rinses, and will be dried, as in an automatic laundry dryer~ The wa~h water will usually be at a temperature of 10 to 95~C., preferably 15 to 60C. or 20 to 50C., and more preferably 40 to 50C., and the concen-tration of the detergent composition or the equivalent components (if separately added to the wash water) will be from 0.05 to 1%, preferably from O.P5 to 0.15%, e.g., 0.06%
or 0.13%. The detergent compositions have a bulk density in the range of 0.2 or 0.4 to 0O9 g./cc., preferably 0.6 to 0.9 g./cc., e.g., 0.65 g./cc. and such detergents of such prefer-red bulk density are normally employed at a concentration of about 1/4 cup (or about 40 grams) per wash, with the wash tub usualiy containing about 17 gallons (U.S.~ of water for top loading machines and about 7 to 8 gallons for front loaders. When a "~uropean" type of washing machine is employed, wherein higher concentrations of detergent composi-tion are utilized, with lesser amounts of water, and which machines usually operate at higher washing temperatures, it may be preferable to lower the washing temperature for best depositing of the polymer on the washed materials. The upper portion of the broad range of de~ergent composition concen-trations previously given may be considered as appropriate for European washing conditions whereas the corresponding L3~

intermediate and lower parts are for "American" type front loading and top loading washers and washing conditions, often with the concentration for the front loading m~chines being lower than that for the top loaders.
The proportions of the individual activè eomponents of the present compositions in the wash water will normally be from 0.001 to 0.14~ of nonionic detergent, 0.006 to 0.40 of builder, 0.0001 to 0.10~ of soil releasing agent and 0.00002 to 0.5~ of PVP. Preferably such proportions will be from 0.003 to 0.02%, ~.02 to 0.05%, 0.0003 to 0.01%, and O.00006 to 0.006%, respectively. When sodium tripolyphosphate and sodium silicate are present in the wash water the normal percentages of the significant components of the present compositions that will be in the wash water are 0.0006 to 0.040% of nonionic detergent, 0.017 to 0.12~ of sodium tripolyphosphate, 0.002 to 0.023~ of sodium silicate, 0.0008 to 0.009% of soil releasing polymer and 0.00013 to 0.004% of PVP, with more preferred ranges being 0.009 to 0.013~, 0.024 to 0.039~, 0.003 to 0.008%, 0.001 to 0.003~, and 0.0002 to 0.0012~, respectively.
The base beads which may be employed in making the compositions of ~he invention are preferably spray dried from an aqueous crutcher mix which normally will contain from about 40 to about 70 or 75~ of solids, preferably 50 to 65~ thereof, with the balance being water, preferably deionized water, as previously described (but city water may also be employed). The crutcher mix i5 preferably made by sequentially adding various components thereof in a manner which will result in the most miscible, readi~y pumpable and non-setting slurry for spray drying~ The order of addition of the materials may be varied, dependiny on the ~ircum-stances, butitis most desirable when "settable" cru~cher mixes are employed to add the silicate solution (if any) last, and if not last, at least after the addition of any gel- or "freeze"-preventing combination of materials or processing aids, such as citric acid and magnesium sulfate.
Normally it is preferable for all or almost all of the water to be added to the crutcher first, preferably at about the processing temperature, after which the processing aids (if present) and other stable minor components, including pig-ment and fluorescent brightener, if present, are added,ollowed by most of the builder~s), including phosphate builder, and silicate builder. Usually during such additions each component will be mixed in thoroughly before addition of the next component but methods of addition may be varied, depending on $he circumstances, so as to allow co-additions when such are feasible. Sometimes component additions may be in two or more par~s and sometimes different components may be pre-mixed before addition, to speed the mixing process. Normally, mixing speed and power will be increased as the materials are added.

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The temperature of thè aqueous medium in the crutcher will usually be about room temperature or elevated, normally being in the 20 to 80C. range, preferably from 30 to 75 or 80C., and more preferably 40 to 70 or 80~C.
~eating the crutcher mediwm may promote solution of the water soluble salts of the mix and thereby increas~ miscibility but the heating operation, when effected in the crutcher, can slow production rates. Temperatures higher than 80C.
(and sometimes those higher than 70C.) will often be avoided because of ~he possibility of decomposition of one or more of possible crutcher mix components, e.g~, ~odium bicarbonateO Also, in some cases lower crutcher temperatures increase the upper limits of crutcher solids contents, probably due to insolubilizing of normally gelling or setting components. Such problems are not usually encountered when the main builder present is a polyphosphate.
Crutcher mixing timeq to ob~ain good slurries can vary widely, from as little as five minutes in small crutchers and for slurries of higher moisture content5, to as much as four hours. The mixing times needed to bring all the crutcher mix components substantially homogeneously together in one medium may be as little as ten minutes but in some cases can take up to an hour, although 30 minutes is a preferable upper limit. Co~nting any such initial admixing times, normally crutching periods will be from 15 minutes to 3~7~

two hours, e.g., 20 minutes to one hour, but the crutcher mix should be such ~s to be mobile, not gelled or set, for at least one hour, preferably for two hours, and more prefer-ably for four hours or longer after completion of the making of the mix. ~he present mixes are stable for at ~east four hours. They do not set during that time when polyphosphate is the main builder, and when carbonate-silicate mixtures are employed an anti-setting agent, such as citric acid plus magnesium sulfate, will be present to delay setting.
The crutchea ~lurry, with the builder salt(s) and other components thereof dissolved or in particulate orm and uniformly distributed therein, is transferred in usual manner to a spray drying tower, which is normally located near the crutcher. The slurry is dropped from the bottom of the crutcher to a positive displacement pump, which orces it at high pressure through spray nozzles at the top of a conventional spray tower (countercurrent or concurrent) wherein the droplets of the slurry fall through a hot drying gas, usually the combustion products of fuel oil or natural gas, in which the droplets are dried to desired bead form.
During drying absorptive beads are made, which are especially useful to absorb liquid state heated nonionic detergent~
which may be post-sprayed onto them subsequently.
After drying,the product is screened to desired size, e.g., 10 to 60 or 100, U.S. Sieve Series, and is ready for application of nonionic detergent spray thereto.

- ~2 -lL3~7~

Although the foregoing description is of the making of spray dried inorganic builder salt base heads, and such are preferred for various reasons already men~ioned, ~uch as desirable bulk density, uniformity, flowability, strength and sorption properties, it is within the invention to employ other equivalent or nearly ~quivalent base beads, such as those which are agglomerates, mixes, granulates, grinds, prills or chopped filamentsO The nonionic detergent will usually be at an elevated temperature, such as 40 to 90~C., preferably 50 to 80C., e.g., 55C., to assure that it will be liquid; yet, upon cooling to room temperature it will desirably be solid, often resembling a waxy solid.
Even if at room temperature the nonionic detergent is slightly tacky, this characteristic does not necessarily make the final composition poorly flowing because the detergent penetrates to below the bead surface (to within the bead). However, waxy detergents are preferred. The nonionic detergent is applied to the moving or tumbling base beads in known manner, as a spray or as droplets. The enzyme preparation (herein referred to as enz~me, although it is recognized that it includes a carrier ma~erial, too), soil releasing polymer, PVP and any other powdered adjuvants may be dusted onto or mixed with the builder base particles, and perfume and any other liquids to be post-added may be sprayed on at ~5 a suitable point before or after addition(s) of the powder(s).

7~

The nonionic detergent may be sprayed onto absorbent base builder beads and the soil release promoting polymer and PVP may be post-added together, with the soil release poly-mer being stabilized by the PVP against the d~grading action of the alkaline builder base beads. Such stabili~ing effect of the PVP is obtained when the release promo~ing polymer and the PVP are in contact, preferably when contact of the xelease polymer and the alkaline builder is also prevented or diminished. However, two particular ways of incorporating - 10 the nonionic detergent, soil release polymer and PVP in the product are highly effective and are preferred. The more preferred method is by spray drying an aqueous crutcher mix of the alkaline builder salt to produce dried absorbent particles, dissolving the formula proportions of soil releasing pol~mer and PVP in nonionic detergent in liquid state, and spraying or otherwise effec~ively distributing the nonionic detergent solution of the release polymer and PVP onto the surfaces of the alkaline builder beads. In carrying out such a procedure it is highly desirable that the nonionic detergent be substantially or essentially anhydrous, normally containing less than 1%, preferably less than 0.5% and more preferably less than 0.2% of moisture. It is preferred that the nonionic detergent be at a temperature in the range of 40 to 90C., more preferably 50 ~o 80~C., at which the 3~

normally solid and waxy detergent will be molten and at which temperature the soil release promoting polymer and the PVP will dissolve in it (in the formula proportions). Also, the base beads will preferably be warmed and are kept in motion, as in a sui able mixer, such a a rotating longitudinal drum or tube which is inclined slightly, e.g., 5 to 10 from the horizontal. The spray droplets will preferably be of a size delivered from a typical spray gun, usually being of a diameter in the range of about 0.1 to 1 mm. The mentioned spraying and mixing can be effected in times as short as one or two minutes but normally from 5 to 10 minutes may be desirable. Surprisingly, although the spraying of the li~uefied nonionic detergent onto the base beads brings the soil release polymer into close contact with such beads and the alkaline bullder salts of which they are composed, apparently due to the presence of the PVP the soil release promoting polymer remains stable on storage, even at somewhat elevated temperatures~ Comparisons with other soil release detergent compositions of similar formulas but without the PVP show that the experimental formulas are far superior in lasting soil release promoting characteristlcs.
Another preferred method for making a detergent composition of this invention includes dissolving the PVP in a li~uid medium, such as water, suitable alcohol, e.g., methanol, or suitable volatile chlorinated organic solvent, L3~

such as methylene chloride. Desirable concentrations of the PVP in the solvent will normally be within the range of 5 to 25%, with higher concentrations preferred when ~olvent removal is more of a problem, as when water is being used.
The solvent solution of PVP is then applied to particulate soil release promoting polymex, with the rate of application being such as to apply the de~ired formula proportion of PVP
to the soil release agent. Thus, for example, when it is desired that the final detergent composition contain 3% of release polymer and 0.5~ of PVP, enough PVP solution will be sprayed or otherwise applied to the surfaces of the particles of the release polymer to produce an intermediate product containing about 86~ of release polymer and about 14% of PVP. Th~ particle sizes of the release polymer will preferably be within the same range as the desired sizes of the nonionic detergent-builder particles of the final detergent composition but other sizes of particles may also be employed, although they will not be as advantageous and may separate out to some extent from the detergent-builder particles. Such detergent-builder particles will be made by spraying the formulapropor~ion of molten nonionic de~ergent onto the absorbent builder salt base beads in a manner like that previously described. Nex~ the two types of particles are blended together and the formula is ready for use. The detergent composition resulting is one in which the release promoting polymer is protected by the PVP from the degrading action of the alkaline builder salt. Additionally, the presence of the nonionic detergent on the builder salt, covering substan-tial portions of the surfaces thereof, further helps to prevent detrimental interactions.
In the applications of PVP to the base beads (with nonionic detergent and release pol~mer) and to the release polymer particles the PVP protects the release polymer from the alkaline builder and furthermore, improves the product otherwise. PVP possesses useful anti-redeposition properties and has been observed to promote stain removal from laundry.
In the present compositions i~ aids in soil release, especially at room temperatures or thereabout, to an extent which is greater than that attributable to stabilization of ; 15 the soil release promoting polymer. A coating of the PVP
helps to protect the detergent composition against the effects of atmospheric moisture~ Yet, PVP is readily soluble in the wash water, leading to quick dissolving and dispersion of the detergent components. Although many o~her products have ~.
been tested, none has been found to give the very desirable effects of PVP, not even other water soluble polymeric amides.
The following examples illustrate the invention but do not limit it. Unless otherwise indicated, all parts are by weight and all temperatures are in C.

3~

Percent Pentasodium tripolyphosphate 54.3 Neodol 23-6.5 (condensation product of 20.7 approximately 6.5 moles of ethylene oxide and a higher fatty alcohol averaging between 12 and 13 carbon atoms per mole) Sodium silicate (Na2O:SiO2 - 1:2.4) 9.58 Moisture 9-05 10 Soil release promoting polymer (a copolymer of 3.00 polyethylene terephthalate and polyoxyethylene terephthlate of a molecular weigh~ of about 22,000 wherein the polyoxye~hylene is of a molecular weight of about 3,400, the molar ratio of polyethylene terephthlate to polyoxyethylene terephthlate units is about 3:1 and the propor-tion of ethylene oxide to phthalic moie~y in the polymer is about 22:1, sold by Alkaril Chemicals, Inc. as Alkaril QCF) 20 Proteolytic enzyme (Maxazyme) 1.32 Fluorescent brightener (Tinopal 5BM) 1.26 Polyvinyl pyrrolidone (GAF Corporation K-15 PVP 0.50 having a molecular weight of about 10,000) Perfume 0.20 25 Dye (Blue, Mix No. 5) 0.05 Dye (Polar Brilliant Blue) 0.04 100. 00 A particulate built nonionic synthetic organic detergent composition of the above formula, which is useful for washing synthetic organic polymeric fibrous materials, such as those of polyesters and polyester-cotton blends, and imparting soil release propertiPs to them, is made by the ~l2~3~7~

following method. First, base beads of the tripolyphosphate and silicate are made by dispersing the tripolyphosphate, as a finely divided powder, in water and adding to it the formula proportion t9.58~) of anhydrous sillcate as a 47.5 S solids solution, with the solids concentration of the crutcher mix made being about 55~. The water employed is deionized but sometimes city water will be substituted, providing that its hardness is less than 300 p.p.m. as calcium carbonate. Preferably, fluorescent brightener and any colorants, such as th~ blue dyes, which are sufficiently~
crutcher stable, are added to the crutcher, too. The crutcher mix is maintained at a temperature in the range of about 60 to 70C. and mixing is continuous. The mixing, including addition and dropping, which are both conducted while mixing, normally takes about 20 minutes to an hour but may be under-taken for longer periods, up to four hours or more, because the phosphate-silicate-dye-brightener dispersion-solution does not tend to set in the crutcher.
After sufficient mixing to obtain a substantially uniform slurry, in which the fluorescent brightener and dyes will often preferably be present, during which time some moisture may be lost by evaporation, and may be replenished, if desired, the mix is dropped from the crutcher to a pump, which pumps it at a pressure of about 21 kg./s~. cm. into the top of a countercurrent spray tower wherein the initial ~2~4374 drying temperature i5 about 430C. and the inal air tempera-ture is about 105C. The base beads resulting are of a bulk density of about 0.5 g./cc. when cooled after manufacture, and are of paxticle sizes in the range of No's. 10 to 100, U.S.
Sieve Series. They may be screened to such range or to a particulate product having fewer smaller particles, ~.g., 10 to 60 sieve. The moisture content of the product is about 12.1%. The base beads are free flowing (generally with about an 80~ flow rate), non-tacky, satisfactorily porous, yet firm on the surfaces thereof and are capable of readily absorbing significant proportions of liquid nonionic detergent ~and dissolved QCF and PVP) without becoming objectionably tacky.
After cooling of the spray dried base beads they are screened so that substantially all (over 95~ and often over 98%) are within the range of No's. 10 to 100 sieve, U.S. Sieve Series, and are sprayed with a solution of QCF
and PVP in anhydrous nonionic detergent, in final product formula proportions. Thus, 0.5 part of the PVP and 3 parts ~f the QCF are dissolved in 20.7 parts of Neodol 23-6.5, which is essentially anhydrous and which is at a temperature of about 71C. and is sprayed onto tumbling base builder bead surfaces, preferably while the beads are being mixed in a tumbling drum, which may be a longitudinal drum or tube inclined to the horizontal at about 8. The spray dr~plets 37~

are largely of particle sizes in the 0.1 to 1 m~. range and the spraying operation will be such as to result in a throughput time in the sprayer-mixer of about 10 to 20 minutes, with the enzyme and perfume being applied in the 5 mixer after the nonionic detergent containing PVP.and QCF.
The resulting detergent composition particlPs, when ~ooled, are of a bulk density of about 0.65 g./cc. The product is attractive and regular in appearance, and is free flowing and non-dusting.
The detergent compositions described above are excellent heavy duty laundry detergents and are especially useful for washing household laundry in automatic washing machines and at the same time imparting soil release character-istics to them. When employed at a temperature of about 45 to 50C. and a concentration of about 0.05 to 0.15~, e.g., 0.06~, in a 17 gallon capacity washer, in the washing of normal loads of 100% polyester and 65% polyester - 35%
cotton fabrics in home laundry or commercial washing machines, whether of the top loading or front loading types, or at higher temperatures and concentrations in European type washing machines, the compositions perform satisfactorily, as would be expected from a knowledge of their components, with respect to usual washing effect characteristics,but additionally they significantly promote soil release from such materials. They are also satisfactory for washing 3~7~

nylons, cottons, acetates and blends of fibrous materials and they promote soil release from such materials too, although not to the same yreat extent as with the poly-esters. In tests of the washing and soil release actions of the compositions a General Electric Company top lQading washing machine or a Terg O-Tometer test washer is used, the water tem-perat~re is about 45~C. and the water contains a total of about 200 p.p.m. hardness as CaC03, of mixed calcium and magnesium ions.
The washing test times are all about ten to fifteen minutes and the laundry : water ratio is about 1:20, by weight.
Items are rinsed twice automatically and then are dried in an automatic laundry dryer or other suitable drying means.
The presence of the PVP with the present soil release promoting polymer significantly stabilizes the release polymer so that with the human eye and by reflecto-meter readings it is evident that be~ter soil release on washing results when a detergent composition comprising the release polymer and PVP is stored for 2 to 4 weeks at elevated temperature and is then used to treat polyesters and polyester-cotton blends, compared to the same product from which the PVP was omitted (not incorporated in the nonionic detergent with QCF) but which was stored and used in the same manner. For better stabilization of the polyester soil release promoter the ratio of PVP to soil release agent should be within the range of 1:15 to 1:2 or 1:1, preferably ~ 32 -3~

1:10 to 1:3, e.g., 1:5 or 1:6. The soil release promoting effect is more significant on repeated launderings, usually up to five launderings of the washed materials, with the pre-sent compositions (or with equivalent wash water ~olutions).
In addition to users of the present pro*~cts noting the in,proved soil release in washing n~rmal loads of laundry containing articles soiled with oils or greases, comparative tests wherein dirty motor oil is applied to swatches sf poly-ester and polyester~cotton blend materials after such swatches have been washed in either the invented compositions or ~ontrol compositions (which are the same as those of the invention but without PVP) show improved soil release promoting for the invented produc~s when both such and the control have been stored at elevated temperatures, e.g , four weeks at 45C.
before being used to wash-treat the swatches. In such tests skilled observers note the improvement in soil removal by washing with a composition of the invention or a control, respectively, after fixst treating and then oil soiling, and such conclusions are confirmed by reflectometer checks of the washed materials. Similar results are obtained when the polyester test materials are washed with the experimental and control detergents, are soiled with dirty motor oil and are then washèd with a commercial detergent, such as a phosphate built anionic detergent of the FAB type.
When variations of the above formulas are made, changing the proportions of soil release polymer and PVP

3~

plus or minus 20% and plus or minus 50%, similar results are obtainable but with the greater proportions of PVP (and release polymer) the soil release effects are better after storage, due to improved stability of the QCF. Similarly, when such changes are made in the builder, nonion~c detergent (to Neodols 25-7 and 23-3) and enzyme components, keeping the formulas within the ranges previously given, useful products result, of improved soil release characteristics despite storage, providing PVP is present. Also, when the PVP is changed to K-30 or K-60 excellent stabilizing of the QCF results, but with K-90 the stability is less. The described results are also obtainable when other polyethylene terephthalate-polyoxyethylene terephthalate copolymers are employed provided that the molecular weights and ratios are within the ranges recited in the specification.

When the compositions of Example l are made by spray drying the base beads, having them absorb a spray of -~
heated nonionic detergent (at 55C.), coating QCF particles in the 10 to 100 sieve range with PVP (K-15? ~o produce particles still in that range, and blending the two partic-ulate intermediate compositions, in the appropriate propor-tions,a stabilized soil release promoting detergent results.
The PVP solution used is at a concentration of about 15~ in methanol, water or methylene chloride, and i~ is applied so - 3~ -~2~37~

as to deposit the formula proportion of PVP on the QCF.
Instead of using an inclined drum mixer a fluid bed dryer (Aeromatic Co.) is employed or the coating of the QCF
particles with PVP, and for evaporation of the solYent.
Although the described coating method is useful and the products resulting are of bulk dencity, detergency and soil release promoting characteristics for lipophilic soils that are comparable to those of the products of Example 1, and are of other good physical characteristics like those of Example 1, it is preferred to employ the absorption method described in Example 1 because it does not require any extra equipment or any additional process steps other than a mixing tank for the dissolving of the QCF and PVP in the nonionic detergent. Also, solvent recovery means are not needed and water evaporation does not have to be effected.

Results like those given in Examples 1 and 2 are also obtainable by use of other compositions, the components of which may be separately added to the wash water at the normal washing temperaturas and concentrations given. While it is preferred to utilize the compositions described, containing nonionic detergent, alkaline builder salt, soil release imparting polyester and PVP or other suitable poly-lactam or polyamide, because the components thereof are in desired proportions and are ready to use, additions sf different partial mixtures of components or individual 7~

components may be made to the wash water, and excellent soil release characteris ics will be acquired by the polyesters and polyester-cotton blend materials being washed (and treated). Of course, when the QCF or similar soil release agent is separate from alkaline builder salt therç will be ~ittle or no need to stabilize the release agent, Still, even in such cases excellent imparting of soil release characteristics is obtainable, employing the same washing conditions as previously mentioned in Examples 1 and 2, and the PVP contributes stain removal and æoil dispersion properties which further help to improve the washing character-istics of the detergent composition solution.
Instead of employing particulate detergent composi-tions, liquids may be utilized, such as more concentra~ed aqueous solutions, such as those of 5 to 25 parts solids, in water or in water and alcholic solvent, and these are especially useful for pre treating before washing any portions of clothing items that are likely to be most soiled by oily materials. Such use is to prevent subsequent hard-to-remove soiling and is particularly appropriate for shirt ~ollars and cuffs, work gloves and aprons, for exampleO The presence of the PVP is considered to help stabilize such liquid preparations but if they are made shortly before intended use such stabilization may not be necessary.
Many variations of the above formulas can be made, utilizing other nonionic detergents, other builders and ~ 3t~

builder combinations, other soil release promoting polymers and other types of PVP, such as have been described in the specification. Also, the various proportions may be changed wi~hin the ranges given, and useful effects of the desired types will result. lt is surprising that the pre~ent composi-tions are so effecti~e and of acceptable and practical stability despite storage at elevated temperatures because PVP is extremely water soluble and would not be expected to "insulate" the soil release agent from atmospheric moisture, which, in the presence of water soluble alkaline salt, would be expected to cause degradation of the release agent.
Also, when nonionic detergent containing dissolved release agent is deposited on base beads of alkaline builder salt it would be expected that the bringing into intimate contact of the alkaline material and the QCF (or QCJ) would promote degradation of the release agent, even in the presence of PVP. Such does not happen, as has been reported above.
Yet, because of the water solubility of the nonionic detergent and its hydrophilicity it would not be expected that it ``
would restrict contact of the alkaline builder salt and the soil release promoter. In short, the present in~ention, in which PVP stabilizes polyester soil release promoting material against alkaline hydrolysis and degradation is unexpected and xepresents an important advance in the detergent axt.

~2~37~

The invention has been described with respect to various examples and illustrations thereof but is not to be considered as limited to these because one of ~kill in the art, with the present specification before him, will be able to utilize substitutes and equivalents without departing from the invention.

Claims

WHAT IS CLAIMED IS:

1. A particulate built nonionic synthetic organic detergent composition for washing synthetic organic polymeric fibrous materials and imparting soil release properties to them which comprises a detersive proportion of a nonionic synthetic organic detergent, a building proportion of a water soluble alkaline builder for such detergent, a soil releasing proportion of a soil releasing polymer of polyethylene tere-phthalate and polyoxyethylene terephthalate, and a stabilizing proportion of polyvinyl pyrrolidone (PVP) for stabilizing the soil releasing polymer in the presence of the alkaline builder.

2. A detergent composition according to claim 1 which comprises from about 5 to 30% of nonionic synthetic organic detergent or a mixture of such detergents, about 30 to 80% of a water soluble alkaline builder salt or a mixture of such salts, about 0.5 to 20% of a soil releasing polymer or a mixture of such polymers and about 0.1 to 10% of PVP.

3. A detergent composition according to claim 2 wherein the nonionic synthetic organic detergent is a condensa-tion product of ethylene oxide and a higher fatty alcohol of 10 to 20 carbon atoms, the builder salt is selected from the group consisting of sodium tripolyphosphate, sodium silicate, sodium pyrophosphate and sodium carbonate, and mixtures thereof, the soil releasing polymer is a polymer of polyethylene terephthalate and polyoxyethylene terephthalate of a molecular weight in the range of about 15,000 to 50,000, wherein the polyoxyethylene of the polyoxyethylene terephthalate is of a molecular weight in the range of about 1,000 to 10,000, with the molar ratio of ethylene terephthalate to polyoxyethylene terephthalate units being within the range of about 2:1 to 6:1, and the PVP is water soluble and of a molecular weight in the range of about 5,000 to 200,000.

4. A detergent composition according to claim 3 wherein the nonionic detergent is a condensation product of a higher fatty alcohol of 12 to 16 carbon atoms with 3 to 20 moles of ethylene oxide per mole of higher fatty alcohol, the builder is sodium tripolyphosphate with sodium silicate of Na2O:SiO2 ratio in the range of 1:1.6 to 1:3, the soil releasing polymer is of a molecular weight in the range of about 19,000 to 43,000, the polyoxyethylene of the polyoxy-ethylene terephthalate thereof is of a molecular weight in the range of about 2,500 to 5,000, the molar ratio of ethylene terephthalate to polyoxyethylene terephthalate units thereof is within the range of 5:2 to 5:1 and the molar ratio of ethylene oxide to phthalic moiety therein is at least 20:1, and the PVP is of a molecular weight in the range of about 10,000 to 160,000, and which composition contains moisture, and the contents of such nonionic detergent, phosphate, silicate, soil releasing polymer, PVP and moisture are within the ranges of 10 to 25%, 30 to 70%, 3 to 15%, 1 to 10%, 0.2 to 5% and 3 to 15%, respectively.

5. A detergent composition according to claim 4 wherein the nonionic detergent is a condensation product of a higher fatty alcohol of 12 to 15 carbon atoms and 6 to 11 moles of ethylene oxide per mole of higher fatty alcohol, the soil releasing polymer is of a molecular weight in the range of 19,000 to 25,000, the polyoxyethylene of the polyoxyethylene terephthalate is of a molecular weight in the range of 3,000 to 4,000, the molar ratio of ethylene terephthalate to polyoxyethylene terephthalate units in the polymers is within the range of 3:1 to 4:1 and the molar ratio of ethylene oxide to phthalic moiety therein is from 20:1 to 30:1, the sodium silicate is of Na2O:SiO2 ratio within the range of 1:2.0 to 1:2.8, and the PVP is of a molecular weight in the range of 10,000 to 50,000, and the contents of nonionic detergent, phosphate, silicate, soil releasing polymer, PVP
and moisture are within the ranges of 15 to 22%, 40 to 65%, 5 to 13%, 2 to 5%, 0.3 to 2% and 5 to 12%, respectively.

6. A detergent composition according to claim 5 wherein the soil releasing polymer is of a weight average molecular weight of about 22,000, the polyoxyethylene of the polyoxyethylene terephthalate is of a molecular weight of about 3,400, the molar ratio of ethylene terephthalate to polyoxyethylene terephthalate units in the polymer is about 3:1 and the molar ratio of ethylene oxide to phthalic moiety therein is about 22:1, the sodium silicate is of Na2O:SiO2 ratio of about 1:2.4, the molecular weight of the PVP is about 10,000 and the contents of such nonionic detergent, phosphate, silicate, soil releasing polymer, PVP and moisture are about 21%, 54%, 10%, 3%, 0.5% and 9%, respectively, with the balance being adjuvants including enzyme, optical bright-ener, colorant and perfume.

7. A process for manufacturing a particulate built nonionic synthetic organic detergent composition for washing synthetic organic polymeric fibrous materials and imparting soil release properties to them, which composition includes a detersive proportion of a nonionic synthetic organic detergent, a building proportion of a water soluble alkaline builder for such detergent, a soil releasing propor-tion of a soil releasing polymer of polyethylene terephthalate and polyoxyethylene terephthalate, and a stabilizing proportion of PVP for stabilizing the soil releasing polymer in the presence of the alkaline builder, which comprises spray drying an aqueous crutcher mix of the alkaline builder to produce dried particles thereof, and applying to such spray dried build-er particles either (i) the nonionic detergent in liquid state containing the soil releasing polymer and the PVP, so that the nonionic detergent, soil releasing polymer and PVP are absorbed by spray dried builder particles, or (ii) the nonionic detergent in liquid state so that it is absorbed by the spray dried build-er particles, applying PVP in a liquid medium to particles of the soil releasing polymer and mixing such resulting particles with the builder particles containing nonionic detergent.

8. A process for manufacturing a particulate built non-ionic synthetic organic detergent composition for washing syn-thetic organic polymeric fibrous materials and imparting soil release properties to them, which composition includes a deter-sive proportion of a nonionic synthetic organic detergent, a building proportion of a water soluble alkaline builder for such detergent, a soil releasing proportion of a soil releasing poly-mer of polyethylene terephthalate and polyoxyethylene tereph-thalate, and a stabilizing proportion of PVP for stabilizing the soil releasing polymer in the presence of the alkaline buil-der, which comprises spray drying an aqueous crutcher mix of the alkaline builder to produce dried particles thereof, and apply-ing to such spray dried builder particles the nonionic detergent in liquid state containing the soil releasing polymer and the PVP, so that the nonionic detergent, soil releasing polymer and PVP are absorbed by the spray dried builder particles.

9. A process according to claim 8 wherein the nonionic detergent is a condensation product of ethylene oxide and a higher fatty alcohol of 10 to 20 carbon atoms, the builder is a salt selected from the group consisting of sodium tripoly-phosphate, sodium silicate, sodium pyrophosphate and sodium carbonate, and mixtures thereof, the soil releasing polymer is a polymer of polyethylene terephthalate and polyoxyethylene terephthalate of a molecular weight in the range of about 15,000 to 50,000 wherein the polyoxyethylene of the polyoxyethylene terephthalate is of a molecular weight in the range of about 1,000 to 10,000, with the molar ratio of ethylene terephthal-ate to polyoxyethylene terephthalate units being in the range of about 2:1 to 6:1, and the PVP is water soluble and of a mol-ecular weight in the range of about 5,000 to 200,000, the pro-portions of nonionic detergent, builder salt, soil releasing polymer and PVP are in the ranges of about 5 to 30%, 30 to 80%, 0.5 to 20% and 0.1 to 10%, respectively, and the soil releasing polymer and PVP are dissolved in the nonionic detergent, which is essentially anhydrous, such solution is at a temperature in the range of 40 to 90°C., and it is sprayed onto the builder salt particles.

43a

10. A process according to claim 9 wherein the nonionic detergent is a condensation product of a higher fatty alcohol of 12 to 16 carbon atoms with 3 to 20 moles of ethylene oxide per mole of higher fatty alcohol, the builder is sodium tripolyphosphate with sodium silicate of Na2O:SiO2 ratio in the range of 1:2.0 to 1:2.8, the soil releasing polymer is of a molecular weight in the range of about 19,000 to 43,000, the polyoxyethylene of the polyoxyethylene terephthalate thereof is of a molecular weight in the range of about 2,500 to 5,000, the molar ratio of ethylene tere-phthalate to polyoxyethylene terephthalate units thereof is within the range of 5:2 to 5:1 and the molar ratio of ethylene oxide to phthalic moiety therein is at least 20:1, and the PVP is of a molecular weight in the range of about 10,000 to 160,000, and which composition contains moisture, and the contents of such nonionic detergent, phosphate, silicate, soil releasing polymer, PVP and moisture in the composition are within the ranges of 10 to 25%, 30 to 70%, 3 to 15%, 1 to 10%, 0.2 to 5% and 3 to 15%, respectively, the spray dried builder particles and the composition particles are of sizes within the range of No's. 10 to 100, U.S. Sieve Series, and are of bulk densities within the range of 0.4 to 0.9 g./cc., and the solution of soil releasing polymer and PVP
in substantially anhydrous liquid state nonionic detergent is at a temperature in the range of 50 to 80°C. when sprayed onto and absorbed by the builder particles and such particles are being kept in motion when such spraying is being effected.

11. A process for manufacturing a particulate built nonionic synthetic organic detergent composition for washing synthetic organic polymeric fibrous materials and imparting soil release properties to them, which composition includes a detersive proportion of a nonionic synthetic organic detergent, a building proportion of a water soluble alkaline builder for such detergent, a soil releasing propor-tion of a soil releasing polymer of polyethylene terephthalate and polyoxyethylene terephthalate, and a stabilizing propor-tion of PVP for stabilizing the soil releasing polymer in the presence of the alkaline builder, which comprises spray dxying an aqueous crutcher mix of the alkaline builder to produce dried particles thereof, applying to such spray dried builder particles the nonionic detergent in liquid state so that it is absorbed by the spray dried builder particles, applying PVP in a liquid medium to particles of the soil releasing polymer and mixing such resulting particles with the builder particles containing nonionic detergent.

12. A process according to claim 11 wherein the nonionic detergent is a condensation product of ethylene oxide and a higher fatty alcohol of 10 to 20 carbon atoms, the builder is a salt selected from the group consisting of sodium tripolyphosphate, sodium silicate, sodium pyrophosphate and sodium carbonate, and mixtures thereof, the soil releasing polymer is a polymer of polyethylene terephthalate and polyoxyethylene terephthalate of a molecular weight in the range of about 15,000 to 50,000 wherein the polyoxyethylene of the polyoxyethylene terephthalate is of a molecular weight in the range of about 1,000 to 10,000, with the molar ratio of ethylene terephthalate to polyoxyethylene terephthalate units being in the range of about 2:1 to 6:1, and the PVP is water soluble and of a molecular weight in the range of about 5,000 to 200,000, the proportions of nonionic detergent, builder salt, soil releasing polymer and PVP are in the ranges of about 5 to 30%, 30 to 80%, 0.5 to 20% and 0.5 to 10%, respectively, the nonionic detergent is essentially anhydrous and is of a temperature in the range of 40 to 90°C., the PVP is in solution in a solvent medium when it is applied to the particles of soil releasing polymer and such solvent is removed from the PVP treated soil releasing polymer before blending of such polymer with the builder particles containing absorbed nonionic detergent.

13. A process according to claim 12 wherein the nonionic detergent is a condensation product of a higher fatty alcohol of 12 to 16 carbon atoms with 3 to 20 moles of ethylene oxide per mole of higher fatty alcohol, the builder is sodium tripolyphosphate with sodium silicate of Na2O:SiO2 ratio in the range of 1:2.0 to 1:2.8, the soil releasing polymer is of a molecular weight in the range of about 19,000 to 43,000, the polyoxyethylene of the polyoxyethylene tere-phthlate thereof is of a molecular weight in the range of about 2,500 to 5,000, the molar ratio of ethylene terephthalate to polyoxyethylene terephthalate units thereof is within the range of 5:2 to 5:1 and the molar ratio of ethylene oxide to phthalic moiety therein is at least 20:1, and the PVP is of a molecular weight in the range of about 10,000 to 160,000, and which composition contains moisture, and the contents of such nonionic detergent, phosphate, silicate, soil releasing polymer, PVP and moisture in the composition are within the ranges of 10 to 25%, 30 to 70%, 3 to 15%, 1 to 10%, 0.2 to 5% and 3 to 15%, respectively, the spray dried builder particles and the detergent composition particles are of sizes within the range of No's. 10 to 100, U.S. Sieve Series, and are of bulk densities within the range of 0.4 to 0.9 g./cc., the nonionic detergent is at a temperature in the range of 50 to 80°C. and is substantially anhydrous when it is applied in the liquid state to the spray dried builder particles, and the applications of such liquid state nonionic detergent to the builder particles and of the PVP in a solvent medium in which it is dissolved to the soil releasing polymer particles are by sprayings of such liquids onto the surfaces of such particles while the particles are being kept in motion.

14. A process for washing synthetic organic polymeric fibrous materials and simultaneously imparting soil release properties to them which comprises washing such a synthetic material in an aqueous medium in a washing machine tub, which medium contains a detersive proportion of a nonionic synthetic organic detergent, a building proportion of a water soluble alkaline builder for such detergent, a soil releasing proportion of a soil releasing polymer of polyethylene terephthalate and polyoxyethylene terephthalate, and a stabilizing proportion of PVP for stabilizing the soil releasing polymer in the presence of the alkaline builder.

15. A process according to claim 14 wherein the nonionic detergent is a condensation product of ethylene oxide in a higher fatty alcohol of 10 to 20 carbon atoms, the builder is a salt selected from the group consisting of sodium tripolyphosphate, sodium silicate, sodium pyrophosphate and sodium carbonate, and mixtures thereof, the soil releasing polymer is a polymer of polyethylene terephthalate and polyoxyethylene terephthalate of a molecular weight in the range of about 15,000 to 50,000, wherein the polyoxyethylene of the polyoxyethylene terephthalate is of a molecular weight in the range of about 1,000 to 10,000, with the molar ratio of ethylene terephthalate to polyoxyethylene terephthalate units being in the range of about 2:1 to 6:1, the PVP is water soluble and of a molecular weight in the range of about 5,000 to 200,000, and the concentrations of the said nonionic detergent, builder salt, soil releasing polymer and PVP in the aqueous medium are in the ranges of about 0.001 to 0.14%, 0.006 to 0.40%, 0.0001 to 0.10%, and 0.00002 to 0.05%, respectively, the washing is of materials made of polyester or polyester-cotton blend and the washing temperature is in the range of 10 to 80°C.

16. A process according to claim 15 wherein the nonionic detergent is a condensation product of a higher fatty alcohol of 12 to 15 carbon atoms and 6 to 11 moles of ethylene oxide per mole of higher fatty alcohol, the builder is sodium tripolyphosphate with sodium silicate of Na2O:SiO2 ratio in the range of 1:2.0 to 1: 2.8, the soil releasing polymer is of a molecular weight in the range of 19,000 to 25,000, the polyoxyethylene of the polyoxyethylene tere-phthalate thereof is of a molecular weight in the range of 3,000 to 4,000, the molar ratio of ethylene terephthalate to polyoxyethylene terephthalate units thereof is within the range of 3:1 to 4:1 and the molar ratio of ethylene oxide to phthalic moiety therein is from 20:1 to 30:1, and the PVP is of a molecular weight in the range of 10,000 to 50,000, and the concentrations of said nonionic detergent, phosphate, silicate, soil releasing polymer and PVP in the aqueous medium are in the ranges of about 0.006 to 0.040%, 0.017 to 0.12%, 0.002 to 0.023%, 0.0008 to 0.009% and 0.00013 to 0.004%, respectively, the washing is of laundry containing items made of polyester or polyester-cotton blends, the washing temperature is in the range of 15 to 60°C. and the laundry is by weight from 2 to 15% of the weight of the aqueous washing medium.