GB2192633A - Endotoxin removal - Google Patents

Endotoxin removal Download PDF

Info

Publication number
GB2192633A
GB2192633A GB08614468A GB8614468A GB2192633A GB 2192633 A GB2192633 A GB 2192633A GB 08614468 A GB08614468 A GB 08614468A GB 8614468 A GB8614468 A GB 8614468A GB 2192633 A GB2192633 A GB 2192633A
Authority
GB
United Kingdom
Prior art keywords
endotoxin
sorbent
solid phase
anticoagulant
polymyxin
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Withdrawn
Application number
GB08614468A
Other versions
GB8614468D0 (en
Inventor
Jonathan Cohen
Calvin John Ryan
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Royal Postgraduate Medical School
Original Assignee
Royal Postgraduate Medical School
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Royal Postgraduate Medical School filed Critical Royal Postgraduate Medical School
Priority to GB08614468A priority Critical patent/GB2192633A/en
Publication of GB8614468D0 publication Critical patent/GB8614468D0/en
Priority to PCT/GB1987/000406 priority patent/WO1987007531A1/en
Publication of GB2192633A publication Critical patent/GB2192633A/en
Withdrawn legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/30Processes for preparing, regenerating, or reactivating
    • B01J20/32Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating
    • B01J20/3231Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating characterised by the coating or impregnating layer
    • B01J20/3242Layers with a functional group, e.g. an affinity material, a ligand, a reactant or a complexing group
    • B01J20/3244Non-macromolecular compounds
    • B01J20/3246Non-macromolecular compounds having a well defined chemical structure
    • B01J20/3248Non-macromolecular compounds having a well defined chemical structure the functional group or the linking, spacer or anchoring group as a whole comprising at least one type of heteroatom selected from a nitrogen, oxygen or sulfur, these atoms not being part of the carrier as such
    • B01J20/3253Non-macromolecular compounds having a well defined chemical structure the functional group or the linking, spacer or anchoring group as a whole comprising at least one type of heteroatom selected from a nitrogen, oxygen or sulfur, these atoms not being part of the carrier as such comprising a cyclic structure not containing any of the heteroatoms nitrogen, oxygen or sulfur, e.g. aromatic structures
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61MDEVICES FOR INTRODUCING MEDIA INTO, OR ONTO, THE BODY; DEVICES FOR TRANSDUCING BODY MEDIA OR FOR TAKING MEDIA FROM THE BODY; DEVICES FOR PRODUCING OR ENDING SLEEP OR STUPOR
    • A61M1/00Suction or pumping devices for medical purposes; Devices for carrying-off, for treatment of, or for carrying-over, body-liquids; Drainage systems
    • A61M1/36Other treatment of blood in a by-pass of the natural circulatory system, e.g. temperature adaptation, irradiation ; Extra-corporeal blood circuits
    • A61M1/3679Other treatment of blood in a by-pass of the natural circulatory system, e.g. temperature adaptation, irradiation ; Extra-corporeal blood circuits by absorption
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/30Processes for preparing, regenerating, or reactivating
    • B01J20/32Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating
    • B01J20/3202Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating characterised by the carrier, support or substrate used for impregnation or coating
    • B01J20/3206Organic carriers, supports or substrates
    • B01J20/3208Polymeric carriers, supports or substrates
    • B01J20/321Polymeric carriers, supports or substrates consisting of a polymer obtained by reactions involving only carbon to carbon unsaturated bonds
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/30Processes for preparing, regenerating, or reactivating
    • B01J20/32Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating
    • B01J20/3202Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating characterised by the carrier, support or substrate used for impregnation or coating
    • B01J20/3206Organic carriers, supports or substrates
    • B01J20/3208Polymeric carriers, supports or substrates
    • B01J20/3212Polymeric carriers, supports or substrates consisting of a polymer obtained by reactions otherwise than involving only carbon to carbon unsaturated bonds
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/30Processes for preparing, regenerating, or reactivating
    • B01J20/32Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating
    • B01J20/3231Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating characterised by the coating or impregnating layer
    • B01J20/3242Layers with a functional group, e.g. an affinity material, a ligand, a reactant or a complexing group
    • B01J20/3244Non-macromolecular compounds
    • B01J20/3246Non-macromolecular compounds having a well defined chemical structure
    • B01J20/3248Non-macromolecular compounds having a well defined chemical structure the functional group or the linking, spacer or anchoring group as a whole comprising at least one type of heteroatom selected from a nitrogen, oxygen or sulfur, these atoms not being part of the carrier as such
    • B01J20/3255Non-macromolecular compounds having a well defined chemical structure the functional group or the linking, spacer or anchoring group as a whole comprising at least one type of heteroatom selected from a nitrogen, oxygen or sulfur, these atoms not being part of the carrier as such comprising a cyclic structure containing at least one of the heteroatoms nitrogen, oxygen or sulfur, e.g. heterocyclic or heteroaromatic structures

Abstract

Endotoxin sorbent comprising a sorbent material selected from the group consisting of polymyxin B and salts, immobilised on a solid phase support, the solid phase-polymyxin B sorbent having been treated with an anticoagulant capable of preventing or limiting fibrin deposition, whereby free anticoagulant binding sites are blocked which may be used to remove endotoxin from endotoxin-containing fluids e.g. from blood in the treatment of gram-negative bacterial shock.

Description

SPECIFICATION Endotoxin removal The present invention relates to the removal of endotoxin from endotoxin-containing fluids.
Endotoxin, which is part of the cell wall of gram negative bacteria, is implicated in gramnegative bacteraemia. This occurs with a frequency of from 4 to 12 per 1000 hospital admissions, and shock as a complication is seen in 16-44% of these cases. The precise pathogenesis of gram-negative bacterial shock, also called septic shock, is unclear, but it is widely held that endotoxin is responsible for many of its features. The overall mortality from septic shock is approximately 60% and has remained at this level for many years, despite improvements in supportive care, more effective antimicrobial agents, the use of corticosteroids and other pharmacological approaches.
Endotoxin is also implicated in various other serious conditions including chronic and acute liver disease, chronic and acute renal disease, radiation sickness and heat stroke.
Polymyxin B is a cyclic polypeptide antibiotic which, in addition to its antimicrobial activity, has been known for many years to have potent anti-endotoxin properties. Polymyxin B (PB) binds stoichiometrically to endotoxin, and will neutralize many endotoxin-induced phenomena including mouse lethality, intravascular coagulation, and the Shwartzman phenomenon. The use of polymyxin B for its anti-endotoxin (rather than anti-microbial) properties has been proposed but the drug is unsuitable for repeated parenteral administration because it is both neurotoxic and nephrotoxic.
An alternative approach that has been proposed is to link polymyxin B to a solid phase support and to use this as a specific sorbent. Polymyxin B has been linked to Sepharose (Trade Mark) and also to polystyrene fibres, and such systems have been found to be capable in vitro of removing endotoxin from endotoxin-containing solutions. The use of fibre-linked polymyxin B has also been described in haemoperfusion of endotoxin-treated dogs, with improved survival in the treated group. There are, however, a number of problems associated with haemoperfusion which reduce its clinical applicability, in particular biocompatibility problems resulting from destruction of cellular elements in the blood (including platelets) during the passage of the blood through the sorbent. The smaller the size of the sorbent particles, the greater is the problem of cell destruction.
The present invention is based on the surprising observation that plasmapheresis of endotoxincontaining blood can be carried out successfully if a solid phase support carrying immobilised polymyxin B is treated before use with an anticoagulant. This observation is surprising because we have attempted to use polymyxin B linked to a solid phase support to remove endotoxin in vivo using the technique of plasmapheresis, but such attempts have failed because of fibrin deposition. This desposition generally starts in the sorbent column within 5 to 10 minutes of starting plasmapheresis and within 15 to 20 minutes the plasmapheresis apparatus as a whole becomes clogged to such an extent that it can no longer function effectively.The fibrin is deposited throughout the plasmapheresis system, not just in the sorption column itself, and the deposition occurs despite the presence of the heparin present conventionally in the circulating plasma.
The present invention provides an endotoxin sorbent comprising polymyxin B immobilised on a solid phase support, the solid phase-polymyxin B sorbent having been treated with an anticoagulant capable of preventing or limiting the deposition of fibrin to block free anticoagulant binding sites.
Polymyxin B may be used as such or in the form of a salt for example, the sulphate. Also there may be used a mixture of any two or more components selected from polymyxin B and salts thereof. Unless otherwise specified, the term "polymyxin B" is used herein to encompass all such possibilities.
The solid phase support may comprise any substance capable of immobilizing polymyxin B. It is thought that in some cases at least polymyxin B can be bound to a support via an amino group, and on this ba#sis the support may be, for example, a solid material capable of forming a covalent bond with an amino group. The polymyxin B may be immobilised on a solid support either directly or via a coupling group. Accordingly, other suitable solid phase support materials are those capable of accepting coupling groups suitable for the immobilisation of polymyxin B.
Examples of solid support materials are agarose and agarose derivatives, other carbohydrates, polystyrene and regenerated cellulose.
The solid phase support may be used in any of a variety of physical forms, such as, for example, those proposed for affinity chromatography in general, for example, beads, fibres, webs, membranes and hollow fibres. Beads, for example, agarose beads, may be used in columns. The size of beads preferred is generally in the range of from 45 to 165jut, but larger or smaller beads may be used, longer columns generally being required with larger diameter beads.
Such bead size/column length parameters will be well-known to those skilled in the art of affinity chromatography. Other physical forms of solid support, for example, fibres, for example, polystyrene fibres, webs, membranes and hollow fibres may be used analogously to their use in affinity chromatography generally.
The anticoagulant used to treat that polymyxin B sorbent must be capable of preventing or limiting the deposition of fibrin, either directly, that is to say, by influencing the conversion of fibrinogen to fibrin, or indirectly, that is to say, by influencing any one or more of the other steps involved in the intrinsic and extrinsic pathways of blood coagulation. Heparin is widely used and known to be effective in preventing fibrin deposition. It is readily available, relatively inexpensive, and substantially free from side effects. Accordingly, heparin is a preferred anticoagulant for the present invention, but any other anticoagulant having the property of interfering with fibrin deposition may be used.
in the heparin-type category are, for example, low molecular weight heparin derivatives and other heparin derivatives. Such derivatives may have advantages over native heparin, for example, with regard to the specificity of their anti-fibrin-deposition activity. Thus, for example, lower molecular weight derivatives may affect platelets less than native heparin does (see, for example, Salzman E.W., Rosenberg R.D., Smith M.H., Linden J.N., and Savreau L., J. Clinical Investigation (1981) 65 64-67). Other strongly acidic substances having a heparin-like anticoagulant effect may be used, for example, dextran sulphate. Hirudin may also be used.
Antithrombotic agents directed towards different aspects of the haemostatic process may be used as the anticoagulant, for example, inhibitors of intrinsic coagulation; and also platelet aggregation inhibitors (antiplatelet agents), for example, adenyl compounds, for example, AMP adenosine and 2-chloroadenosine; dipyridamole and lidoflazine; prostacyclin and prostaglandin E; anti-inflammatory drugs, for example, aspirin, phenylbutazone, indomethacin, meclofenamate and hydroxychloroquine; membrane stabilizers, for example, local anaesthetics and many antihistamines; serotonin antagonists; sulphydryl inhibitors, for example, N-ethylmaleimide and p-hydroxymercuribenzoate; arginine esters and other guanidino compounds; various miscellaneous drugs which inhibit platelet aggregation, for example, clofibrate, methylxanthines, and monoamine oxidase inhibitors and also plasminogen activators, which enhance fibrinolysis, for example, plasmin, streptokinase, and urokinase.
The present invention further provides a process for producing anticoagulant-treated, solid phase-immobilised polymyxin B, which comprises immobilising polymyxin B on a solid phase support and subsequently treating the solid phase support carrying polymyxin B with an anticoagulant capable of preventing or limiting fibrin deposition under conditions such that free anticoagulant binding sites are blocked.
The anticoagulant treatment of the solid component may be carried out by incubating a sample of the polymyxin B-bearing solid phase support with a predetermined volume of a solution comprising the anticoagulant, or an anticoagulant-containing solution may be passed over and/or through a sample of the polymyxin B-bearing solid phase component.
As indicated above, a wide variety of substances may be used as the solid phase support, and polymyxin B may be immobilised on the support in a conventional manner. In the case of agarose, available commercially as in bead form "Sepharose", the agarose is activated, for example, using cyanogen bromide, and then reacted with polymyxin B, for example, according to the method of lssekutz (J. Immunological Methods 61 (1983) 275-281). According to this method, all reactions should be carried out in a pyrogen-free environment, that is to say, the buffers and reagents should be prepared in a sterile fashion using pyrogen-free water, glass-ware should be rendered as pyrogen-free as possible, and sterile plasticware should be used whenever practicable.Materials of the "Sepharose" type can be activated with cyanogen-bromide in a conventional manner, or Sepharose itself can be obtained in activated form from the manufacturers (Pharmacia, Uppsala, Sweden). The activated material is generally swollen, washed, for example, in 0.1 M HCI, and suspended in a suitable buffer, for example, a sodium bicarbonate buffer, for example, 0.1 M NaHCO3 containing 0.5 M NaCI, final pH 8.3. The resulting gel is preferably allowed to settle, excess buffer removed, and then polymyxin B, generally in the form of polymyxin B sulphate, is added to the gel, generally in the form of a solution in a buffer, for example, as described above.The mixture of polymyxin B and the agarose material, for example, Sepharose, is allowed to react for a suitable time, for example, overnight, at a temperature generally between 0 C and room temperature, for example, in the range of from 20C to 18 C, for example, 4"C. Excess buffer is then generally discarded. At this stage it is conventional to incubate the gel with an agent capable of blocking remaining reactive groups, for example, ethanolamine.
In the case of other solid phase support materials, the polymyxin B may be immobilised in an analogous or conventional manner. The immobilisation of polymyxin B on polystyrene fibres has been described by Endo et al (Abstracts of the 14th International Congress of Chemotherapy 1985, Kyoto, Japan, Abstract P-40-9, International Society of Chemotherapy, active halogen method), and also by Hanasawa et al (Therapeutic Aphersis: A critical look. Nose Y, Malchesky P.S., Smith JW, ISAO Press, Cleveland 1984 pp 164-170).
As indicated above treatment of the solid phase support on which polymyxin B has been immobilised with the anticoagulant may be carried out by incubating the solid component with a solution comprising the anti-coagulant. A range of temperatures may be used, for example, from 20C to 25 C, but room temperature is generally suitable.
The amount of anticoagulant used and the time of incubation is such that free anticoagulant binding sites on the solid component are blocked. Clearly, the number of free anticoagulant binding sites will vary depending on the chemical constitution and physical form of the solid, and on the loading with polymyxin B. Having appreciated that the sites, and preferably as many as possible, should be blocked, it is a matter of simple trial and error to determine appropriate amounts of anticoagulant and incubation times. It is generally convenient to use an excess, preferably a considerable excess, of the anticoagulant compared with the amount generally incorporated in saline to prime plasmapheresis apparatus before use. In the case of heparin, this priming amount is generally within the range of from 5 to 20 units of heparin per ml of saline, for example, 10 units of heparin per ml.
As a guide, a suitable amount of anticoagulant in a plasmapheresis system for removing endotoxin from blood where the anticoagulant is heparin, the solid phase is Sepharose 4B beads having a diameter within the range of from 45 to 1 65#, and the amount of polymyxin B incubated with the Sepharose is 50 mg per 1.6 g dry weight, is 1,000 or more units of heparin per ml of Sehparose gel. Amounts of heparin as low as 100 units per ml of Sepharose gel wil give satisfactory results for a short time but after 30 to 40 minutes fibrin deposition in the extracorporeal circulation is observed. Accordingly, amounts of heparin in excess of 100 units per ml Sepharose gel are recommended, preferably 500 units or more, and especially 1,000 units or more, for example, 5,000 units or more, for example, 10,000 units.
The amounts of heparin required for other systems may be determined readily by simple trial and error but, as indicated above, it is generally convenient to use an excess, and preferably a large excess, and these considerations apply, mutatis mutandis, to other chosen anticoagulants.
As indicated above, instead of treating a batch of polymyxin B-bearing solid phase support with a predetermined volume of anticoagulant-containing solution, the solution may be passed over and/or through the batch of solid component. Again, the amount of anticoagulant to be used may be determined by simple trial and error and the considerations given above with regard to the amount of anticoagulant to be used also apply to present embodiment of the invention.
There is preferably used an excess, especially a large excess, of anticoagulants especially heparin compared with the amount generally incorporated in saline for the purpose of priming plasmapheresis apparatus before use. The guide values given above for heparin may be followed. The perfusion of the polymyxin B-bearing solid phase support with anticoagulant-containing solution may be carried out as a separate step before incorporation of the treated material in plasmapheresis apparatus, or the perfusion may be carried out in situ in plasmapheresis apparatus before use, that is to say, before connection to the subject to be treated.
The resulting anticoagulant-treated endotoxin sorbent may be prepared in advance and stored before use, for example, in pyrogen-free water containing a suitable preservative, for example, 25% (v/v) ethanol, or 0.2% (w/v) sodium azide, or it may be prepared as required, for example, in situ as described above.
As indicated above, the resulting anticoagulant-treated endotoxin sorbent may be incorporated in suitable plasmapheresis apparatus, and the present invention also provides an endotoxin sorbent according to the present invention in a form suitable for use in plasmapheresis apparatus, for example, in a chromatography column, and the present invention further provides plasmapheresis apparatus including an anticoagulant-treated polymyxin B-carrying solid phase support according to the present invention.
Surgical techniques for the insertion into a body of lines suitable for the removal and return of blood to be treated by plasmapheresis are known. The blood removed is generally pumped through a plasma separator within which the plasma is separated from the cellular components of the blood. In one method of plasmapheresis, the separated plasma is discarded, and the cellular components of the blood are returned to the body with replacement plasma or plasma substitute. In another method, the separated plasma is passed through sorbent means comprising a sorbent material to adsorb or absorb certain materials either non-specifically or specifically.
The treated plasma is then reunited with the cellular blood components and returned to the body. The sorbent material may be a non-specific sorbent material, for example, powdered charcoal, or may comprise material -suitable for affinity chromatography. The sorbent material is conventionally present in the form of a column. Before carrying out plasmapheresis, the extracorporeal circuit should be primed with anticoagulant-containing solution, for example, heparincontaining saline, for example, saline containing 10 units of heparin per ml, or donor plasma containing 10 units of heparin per ml.
The present invention provides a method of removing endotoxin from endotoxin-containing blood, which comprises separating plasma from the cellular components of the blood, and treating the plasma with an endotoxin sorbent according to the present invention.
The separation of the plasma and its subsequent treatment with the endotoxin sorbent may be carried out in the same apparatus or the separated plasma may be treated in a separate endotoxin sorbent-containing apparatus.
The method of removing endotoxin from endotoxin-containing blood comprises, for example, subjecting the blood to plasmapheresis in apparatus comprising anticoagulant-treated, polymyxin B-bearing solid phase support according to the present invention as a sorbent means.
The second method of plasmapheresis described above may be used in the present invention, that is to say, the method whereby the separated plasma is treated with sorbent means, reunited with the cellular components and returned to the body. In this case, separated plasma is treated "on line" with the sorbent means.
Alternatively, plasma may be separated from endotoxin-containing whole blood by plasmapheresis then treated on separate apparatus, for example, a column comprising an endotoxin sorbent according to the invention. The treated plasma may then if desired, be reunited with the cellular components of the blood, before return to the body. The method of the present invention includes both of these embodiments.
In plasmapheresis apparatus comprising sorbent means, the sorbent means may be any of the forms of anticoagulant-treated, polymyxin B-bearing solid phase support described above. The sorbent means is preferably in the form of a column, and the solid support is especially agarose or polystyrene. The anticoagulant is especially heparin.
The sorbent means may be pre-treated with the same anticoagulant as is used to prime the extra-corporeal circuit, or a different anticoagulant may be used. It is preferable to use the same agent both for pre-treatment of the solid support and for priming the extra-corporeal circuit.
Heparin is preferably used.
Alternatively, as indicated above, the sorbent means incorporated in the plasmapheresis apparatus may be polymyxin B-bearing solid phase support that is treated in situ with anticoagulant.
The amount of anticoagulant to be circulated through the solid component is indicated above, and should be an excess, especially a large excess compared with the amount of anticoagulant used conventionally for priming plasmapheresis apparatus, for example, in the case of heparin with agarose beads (in the form of Sepharose 4B), amounts of heparin in excess of 100 units per ml agarose gel are recommended, preferably 500 units or more, and especially 1,000 units or more, for example, 5,000 units or more, for example, 10,000 units.
The endotoxin-removal component of the plasmapheresis apparatus may be used in conjunction with one or more other components suitable for removing substances from plasma, either specifically or non-specifically, that is to say, one or more other sorbent means. These other components may be used in series or in parallel with the endotoxin-removing component.
Examples of components for removing other substances from plasma are activated charcoal, broadbased sorbents used in the treatment of acute poisoning, chronic and acute renal failure; particles suitable for the removal of non-polar solutes from polar media for example, plasma; non-ionic macroreticular resins; sorbents with a particular attraction for lipid-soluble molecules; anionic exchange resins; sorbents suitable for the removal of protein-bound solutes, for example, bound antibodies having a selective removal action; artificial cells; and immobilised or encapsulated enzymes.
In some cases, it may be possible to immobilise another sorbent, for example, certain of those described above, on the same solid phase support as the polymyxin B. The present invention includes such mixed sorbents.
After use, some or all of the endotoxin may be removed from the sorbent using certain buffer systems, for example, a solution containing deoxycholate, for example, 1% (w/v) deoxycholate, thus regenerating the 1% sorbent. For clinical use, however, it is advisable to use fresh rather than regenerated sorbent material.
The efficacy of the anticoagulant-treated polymyxin B bearing solid phase support as sorbent in the removal of endotoxin can be tested in vitro. There are various assays which can be used for determining endotoxin levels, for example, those using Limulus amoebocyte lysate. There are various modifications of this assay, (see for example Cohen and McConnell (J. Infect. Dis 1984 50 916-924). Assay kits for Limulus amoebocyte lysate gelation tests are available commercially.
Polymyxin B may be assayed in a conventional manner, for example, using the standard bioassay which employs Bordetella bronchiseptica ATCC 4617 (see Sullman S.C. Polymyxins In: Reeves D.S., Philips I., Williams J.D. and Wise R., Laboratory methods in antimicrobial chemotherapy, 1st Ed. Churchill-Livingstone, 1978, 232-234).
The assay methods described above may also be used in connection with plasmapheresis.
It has been found that the polymyxin B remains substantially immobilised on the solid phase - support and is not eluted off during treatment of plasma. This is an important advantage, as polymyxin B is neurotoxic and nephrotoxic.
It will be appreciated that, although the invention has been described above in terms of polymyxin B, it is applicable to all endotoxin sorbents. Accordingly, the present invention also provides endotoxin sorbent immobilised on a solid phase support, the solid phase-endotoxin sorbent having been treated with an anticoagulant capable of preventing or limiting fibrin desposition, whereby free anticoagulant binding sites are blocked, apparatus comprising the sorbent and a method of removing endtoxin from blood using the sorbent.
The following Examples illustrate the present invention. In the Examples, percentages are calculated as w/v, unless otherwise specified.
Example 1 a. Preparation of PB-Sepharose. (Polymyxin B-Sepharose).
The method described by Issekutz (loc cit) was followed. Sterile pyrogen-free plasticware was used whenever practicable. Glassware was washed thoroughly and heated at 1 600C overnight before use. All buffers and reagents were prepared in a sterile fashion and were pyrogen-free, 1.6 g of cyanogen bromide activated Sepharose 4B (Pharmacia, Uppsala, Sweden) was washed extensively in 1 mM HCI and then resuspended in coupling buffer (0.1 M NaHCO3 containing 0.5 M NaCI, final pH 8.3.) The gel was allowed to settle, and excess buffer was removed and replaced with 2.5 ml of the above coupling buffer containing 50 mg of PB (Calmic Medical, London England). (For control columns, PB was omitted).The tube containing the Sepharose was then sealed and incubated at 4 C, for 18 hours on a mechanical rotator. Next, the gel was centrifuged at 80 9 and excess buffer removed. Ten ml of 1 M ethanolamine pH7 were added and the tube incubated for 2 hours at room temperature. After further gentle centrifugation the supernatant was removed and the gel washed in three alternating cycles of acetate buffer (0.1 M sodium acetate with 0.5 M NaCI, final pH 4.0) and borate buffer (0.1 M sodium tetraborate with 0.5 M NaCI final pH 8.0). Finally, the gel was incubated on a rotary mixer for 1.5 hours at room temperature with heparinized sterile 0.9% saline using 10,000 units of heparin per ml of gel. The treated gel was washed with 0.9% saline and was stored at 40C in 0.9% saline containing 0.02% sodium azide.
b. Endotoxin assay.
There was used a modified quantitative chromogenic Limulus amoebocyte lysate (LAL) assay, as described previously (Cohen and McConnell, loc cit). This method was further modified; the lysate was used at a 1 in 10 dilution in pyrogen-free water of the strength recommended by the manufacturers. (MA Bioproducts, Walkersville, Md, USA). The chromogenic substrate was S2423 (Kabi Diagnostica, Stockholm, Sweden).
c. Polymyxin B assay.
A standard bioassay which employs Bordetella bronchiseptica ATCC 4617 (Sullmann S.C. loc cit) was used.
d. Experimental procedure.
One millilitre of PB-Sepharose (or antibiotic-free control Sepharose: CON-Sepharose) was washed with 20 ml of 0.9% saline and incubated for 30 minutes at room temperature with 5000 mg of endotoxin derived from Escherichia coli 0127: B8 (Sigma, Poole, Dorset UK). The suspension was placed in a 2 ml sterile plastic syringe pre-packed with a small wad of glass wool. The column was washed with sterile 0.9% saline and six sequential 1 ml fractions collected over 30 minutes. The amount of endotoxin in each fraction was determined as described above. The experiment was carried out five times for both PB-Sepharose and CON Sepharose.
Additionally, 10 ml of 0.9% saline were run three times through PB-Sepharose or CON Sepharose columns, then bioassayed for PB.
Example 2 a. Plasmapheresis.
The surgical technique for insertion of indwelling carotid arterial and jugular venous lines, allowing perfusion in the unrestrained and conscious state was as previously described (Ryan C.J., Pusey C.D., Aslam M, Gaylor J.D., Maini R., and Courtney J.M., Artificial Organs Vol. 10, No. 2, 135-144 (1986).
Plasmapheresis apparatus is described, by way of example only, with reference to Figure 1, which is a diagrammatic representation. A rat 1 to which indwelling carotid arterial and jugular venous lines 2 and 3 respectively had been inserted was kept in a container 4 and given food and water ad libitum. The arterial blood is pumped, by a pump 5, through a specially designed plasma separator into a reservoir 7. The filtered plasma is pumped by a pump 8 through a column 9 containing the sorbent material. The treated plasma is then reunited with the cellular blood components in a mixing means 10 and returned pumped by pump 11 to the animal via jugular vein lines. Using a 3 pump system trans-membrane pressure can be maintained at less than 50 mmHg with a filtration rate of 0.2-0.22 ml/min. By these means, one complete plasma volume (approximately 11-12 ml) can be treated in 50-60 minutes.The extracorporeal circuit is primed with approximately 3 ml of heparinized saline, obviating the need for donor blood or plasma. Previous studies in 15 normal animals have established that the system can be used repeatedly with no apparent side effects, nor marked effects on red cell, leucocyte or platelet counts. A sieving coefficient of > 98% for the plasma membrane was obtained for C3, IgC and albumen.
b. Clearance of endotoxin.
Two groups of 3 rats were studied. Twenty-one hours following cannulation, lead acetate 50 mg/kg was given intravenously (Selye H., Tuchweber B., and Bertok L., J. Bact. (1966) 91 884-890), and 45 minutes later the animals received endotoxin 10 ,ug/kg intra-arterially. After a further 15 minutes plasmapheresis as described in (a) above was begun and continued for 90 minutes, in one group using PB-Sepharose columns and in the other, CON-Sepherose. Plasma samples for endotoxin measurement were obtained simultaneously from 3-way tape [ 10 and 11 ] placed immediately beneath ('pre') and above ('post') the column, respectively.
To determine the effect of the lead acetate, two rats were studied as described above, except that they received 1 ml of 0.9% saline instead of endotoxin. Serial blood samples were obtained, and the animals were observed for 24 hours. In addition, an aliguot of each plasma sample was mixed in vitro with endotoxin to give a fixed final concentration of 50 ng/ml. These samples were assayed to determine if plasma containing lead acetate inhibited the detection of endotoxin in the LAL assay.
c. Effects of endotoxin removal.
An additional two groups of 4 rats received lead acetate and endotoxin as described above and then underwent plasmapheresis as described above using either PB-Sepharose or CON Sepharose columns. Blood samples were obtained prior to injection of endotoxin, immediately before plasmapheresis, and at intervals thereafter for estimation of haemoglobin, packed cell volume and leucocyte count using a Coulter Counter model 2F; platelet counts were determined manually. The animals were observed for 24 hours.
Plasma from four PB-Sepharose perfused animals was used to determine if PB was eluted from the column in vivo. Samples obtained at 5, 10 and 15 minutes and at 90, 120 and 240 minutes were pooled and assayed for PB as described.
d. Statistical methods In vitro clearance of endotoxin on PB-Sepharose or CON-Sepharose colums was compared by Students' T-test. The effect of plasmapheresis on leucocyte and platelet counts was examined by analysis of variance.
e. Results (1). In vitro studies.
Figure 2 illustrates the cumulative recovery of endotoxin in 6 x 1 fractions collected from CON Sepharose and PB-Sepharose columns. Twenty-four per cent of the challenge dose (5,000 ng) remained on the control column, compared to 94% on the PB-Sepharose column (p=0.05).
There was no detectable anti-microbial activity in the 0.9% saline washed through the PB Sepharose column. The B. bronchiseptica assay could detect 10 #/ml of PB.
(2). In vivo studies.
Plasma endotoxin levels measured 'pre' and 'post' the PB-Sepharose and CON-Sepharose columns after injection of 10mg/g endotoxin followed by plasmapheresis are shown in Figure 3.
In the control animals, the peak level reached at 20 minutes was 260 ng/ml. The 'pre' and 'post' column endotoxin levels were the same, indicating that there was no significant endotoxin clearance across the CON-Sepharose column. In animals perfused over PB-Sepharose, the peak 'pre' column level, which occurred at 30 minutes, was 50 ng/ml. Moreover, the peak 'post' column endotoxin concentration was 13 ng/ml, and for most of the remainder of the experiment was undetectable. It is of interest that endotoxin was present continually in 'pre' column samples from PB-Sepharose treated animals, despite the fact that endotoxin was undetectable in 'post' column samples for most of the experiment. Thus, the absorbent was effectively removing the endotoxin presented to it, but it appeared that further endotoxin (albeit at a low level) was being generated from the animal. The most plausible explanation is that this 'fresh' endotoxin is derived from the intestinal microflora.
Control animals that received lead acetate alone remained well throughout 24 hours of observation, and serial blood samples revealed no change in haemoglobin, leucocyte or platelet counts. The presence of lead acetate in the plasma did not impair endotoxin detection in the LAL assay (data not shown). Pooled plasma samples from 4 PB-Sepharose animals contained no detectable PB activity.
The effect of PB-Sepharose perfusion on endotoxin-induced leucopenia is shown in Figure 4.
The total leucocyte count fell from 7.15+3.9x109/L immediately prior to plasmapheresis, to 6.25+1.5x109/L after 4 hours. In animals perfused over CON-Sepharose, the leucocyte count fell from 5.7+1.3x109/1 to 2.5+1.0x109/L (p 0.01).
Figure 5 illustrates the effect of the procedure on the platelet count. Animals perfused over the PB-Sepharose were protected substantially from thrombocytopenia: the initial count was 550 + 37 x 109/L, and it fell to 430+29x109/L. In control animals, the count fell from 546#130;; 109/L to 108+45;; 109/L (p 0.001) All four control animals died 5-10 hours after the procedure began. In contrast, all four animals perfused over PB-Sepharose survived the 24 hour observation period.
Unequivocal evidence was obtained to show that the PB-Sepharose-treated animals were protected from endotoxin-induced leucopenia, thrombocytopenia and death.
It was important to establish if these observations were indeed the result of selective endotoxin removal or whether there could be an alternative explanation, in particular, whether PB was leaking from the column and neutralizing the endotoxin in the fluid phase. Using a sensitive bioassay for PB, there was found no detectable antimicrobial activity either in eluates obtained after extensive in vitro washing, or in pooled plasma samples from animals perfused over PB Sepharose. The possibility cannot be excluded that very small amounts of PB were eluted from the column, but if so the antibiotic would be present at concentrations considerably less than the typical peak serum level of 2-8 mg/l (20-80,000 ,u/l).

Claims (26)

1. An endotoxin sorbent comprising polymyxin B or a salt thereof immobilised on a solid phase supprt, the solid phase-polymyxin B sorbent having been treated with an anticoagulant capable of preventing or limiting the deposition of fibrin, whereby free anticoagulant binding sites are blocked.
2. An endotoxin sorbent as claimed in claim 1, wherein the anticoagulant as heparin, a low molecular weight heparin derivative, or hirudin.
3. An endotoxin sorbent as claimed in claim 1, wherein the anticoagulant is an inhibitor of intrinsic coagulation, a platelet aggregation inhibitor, or a plasminogen activator.
4. An endotoxin sorbent as claimed in any one of claims 1 to 3, wherein the solid phase support is a material capable of forming a covalent bond with an amino group, or capable of accepting a coupling group suitable for the immobilisation of polymyxin B.
5. An endotoxin sorbent as claimed in any one of claims 1 to 3, wherein the solid phase support is agarose or a derivative thereof.
6. An endotoxin sorbent as claimed in any one of claims 1 to 3, wherein the solid phase support is polystyrene.
7. An endotoxin sorbent as claimed in any one of claims 1 to 6, wherein the solid phase support is in the form of beads, fibres, hollow fibres, webs or membranes.
8. An endotoxin sorbent as claimed in claim 1, wherein the solid phase support is agarose and the anticoagulant is heparin.
9. An endotoxin sorbent as claimed in claim 1, substantially as described in Example 1 herein.
10. A process for producing an endotoxin sorbent as claimed in claim 1, which comprises immobilising polymyxin B or a salt thereof on a solid phase support, and subsequently treating the solid phase support carrying polymyxin B or a salt thereof with an anticoagulant capable of preventing or limiting the deposition of fibrin, under conditions such that free anticoagulantbinding sites are blocked.
11. A process as claimed in claim 10, wherein the solid phase support carrying polymyxin B is incubated with a predetermined volume of a solution comprising the anticoagulant.
12. A process as claimed in claim 10, wherein a solution comprising the anticoagulant is passed over and/or through the solid phase support carrying polymyxin B or a salt thereof.
13. A process as claimed in any one of claims 10 to 12, wherein the solid phase support is as defined in any one of claims 4 to 7.
14. A process as claimed in any one of claims 10 to 13, wherein the anticoagulant is as defined in claim 2 or claim 3.
15. A process as claimed in claim 10, claim 11 or claim 12, wherein the solid phase support is agarose and the anticoagulant is heparin.
16. A process as claimed in claim 10, carried out substantially as described in Example 1 or Example 2 herein.
17. An endotoxin sorbent as claimed in claim 1, whenever produced by a process as claimed in any one of claims 10 to 16.
18. An endotoxin sorbent as claimed in any one of claims 1 to 9 or claim 17 in a column suitable for use in plasmapheresis or affinity chromatography apparatus.
19. An endotoxin sorbent as claimed in claim 18, substantially as described in Example 2 herein.
20. Plasmapheresis apparatus which includes an endotoxin sorbent as claimed in any one of claims 1 to 9 and 17 to 19.
21. Plasmapheresis apparatus as claimed in claim 20, wherein the endotoxin sorbent is produced in situ by passing a solution comprising the anticoagulant over and/or through the solid phase support carrying immobilised polymyxin B or a salt thereof to block anticoagulant binding sites.
22. Plasmapheresis apparatus as claimed in claim 20 or claim 21, which also comprises one or more other sorbents.
23. Plasmapheresis apparatus as claimed in claim 22, wherein the other sorbent is or are selected from activated charcoal; broad-based sorbents used in the treatment of acute poisoning or chronic or acute renal or liver disease; particles suitable for the removal of non-polar solutes from plasma; non-ionic macroreticular resins; sorbents having a particular attraction for lipidsoluble molecules; anionic exchange resins; sorbents suitable for the removal of protein-bound solutes; immunoadsorbents; and immobilised encapsulated enzymes.
24. Plasmapheresis apparatus as claimed in claim 22 or claim 23, wherein the other sorbent means is in series or in parallel with the endotoxin sorbent, or is carried on the same solid phase support as the polymyxin B.
25. Plasmapheresis apparatus substantially as described herein with reference to, and as illustrated by, Fig. 1 of the accompanying drawings.
26. Endotoxin sorbent immobilised silicon immobilised on a solid phase support, the solid phase-endotoxin sorbent having been treated with an anticoagulant capable of preventing or limiting fibrin deposition, whereby free anticoagulant binding sites are blocked.
GB08614468A 1986-06-13 1986-06-13 Endotoxin removal Withdrawn GB2192633A (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
GB08614468A GB2192633A (en) 1986-06-13 1986-06-13 Endotoxin removal
PCT/GB1987/000406 WO1987007531A1 (en) 1986-06-13 1987-06-11 Endotoxin removal

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB08614468A GB2192633A (en) 1986-06-13 1986-06-13 Endotoxin removal

Publications (2)

Publication Number Publication Date
GB8614468D0 GB8614468D0 (en) 1986-07-16
GB2192633A true GB2192633A (en) 1988-01-20

Family

ID=10599433

Family Applications (1)

Application Number Title Priority Date Filing Date
GB08614468A Withdrawn GB2192633A (en) 1986-06-13 1986-06-13 Endotoxin removal

Country Status (2)

Country Link
GB (1) GB2192633A (en)
WO (1) WO1987007531A1 (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6803183B2 (en) 2002-07-18 2004-10-12 Clarigen, Inc. Method for removing pyrogens from plasma and blood for treatment of septic shock
US7585620B2 (en) 2002-06-24 2009-09-08 Profos Ag Method for identifying and for extracting endotoxin
US8003313B2 (en) 2005-01-21 2011-08-23 Hyglos Invest Gmbh Method for detecting and removing endotoxin
US11472836B2 (en) 2013-02-26 2022-10-18 Emd Millipore Corporation Selective removal of a protein from a mixture of proteins using activated carbon by adjusting solution conditions

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0328256A1 (en) * 1988-01-21 1989-08-16 Owens-Corning Fiberglas Corporation Glass fibers coated with agarose for use as column packing or chromatographic media for bioseparations
WO1989009627A1 (en) * 1988-04-07 1989-10-19 Edward Shanbrom Non-thrombogenic intravascular catheter coated with polymyxin
US7799347B2 (en) * 2006-09-07 2010-09-21 Chondrex Inc. Endotoxin-adsorbent for the prevention and treatment of autoimmune diseases
PL2115010T3 (en) 2007-02-28 2012-07-31 Lipoxen Tech Limited Reduction of endotoxin in polysialic acids
DE102015002073A1 (en) * 2015-02-18 2016-08-18 Fresenius Medical Care Deutschland Gmbh Apparatus for carrying out apheresis treatment
CN112552500B (en) * 2021-01-04 2022-12-20 珠海麦得发生物科技股份有限公司 Method for removing endotoxin in PHAs by fermentation method

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CA1221307A (en) * 1982-12-02 1987-05-05 Nobutaka Tani Adsorbent and process for preparing the same
JPH0738880B2 (en) * 1983-06-24 1995-05-01 東レ株式会社 Endotoxemia treatment

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7585620B2 (en) 2002-06-24 2009-09-08 Profos Ag Method for identifying and for extracting endotoxin
US7858299B2 (en) 2002-06-24 2010-12-28 Hyglos Invest Gmbh Method for detecting and for removing endotoxin
US6803183B2 (en) 2002-07-18 2004-10-12 Clarigen, Inc. Method for removing pyrogens from plasma and blood for treatment of septic shock
US8003313B2 (en) 2005-01-21 2011-08-23 Hyglos Invest Gmbh Method for detecting and removing endotoxin
US8329393B2 (en) 2005-01-21 2012-12-11 Hyglos Invest Gmbh Method for detecting and removing endotoxin
US8822641B2 (en) 2005-01-21 2014-09-02 Hyglos Invest Gmbh Method for detecting and removing endotoxin
US9229002B2 (en) 2005-01-21 2016-01-05 Hyglos Invest Gmbh Nucleic acids encoding bacteriophage tail proteins
US11472836B2 (en) 2013-02-26 2022-10-18 Emd Millipore Corporation Selective removal of a protein from a mixture of proteins using activated carbon by adjusting solution conditions

Also Published As

Publication number Publication date
GB8614468D0 (en) 1986-07-16
WO1987007531A1 (en) 1987-12-17

Similar Documents

Publication Publication Date Title
Langer et al. An enzymatic system for removing heparin in extracorporeal therapy
JP2929516B2 (en) Method for quantitatively and selectively removing or / and preparatively preparing tumor necrosis factor and / or lipopolysaccharide from aqueous liquid, apparatus and apparatus unit for removing tumor necrosis factor and / or lipopolysaccharide from liquid in vitro And adsorption material
Chenoweth et al. Anaphylatoxin formation during hemodialysis: Comparison of new and re-used dialyzers
Hammerschmidt et al. Complement-induced granulocyte aggregation in vivo.
Chenoweth Complement activation during hemodialysis: clinical observations, proposed mechanisms, and theoretical implications
Hammerschmidt et al. Complement activation and neutropenia occurring during cardiopulmonary bypass
JP5858299B2 (en) A new adsorbent for endotoxin.
Cohen et al. Protection from endotoxemia: a rat model of plasmapheresis and specific adsorption with polymyxin B
JP5656871B2 (en) Endotoxin sorbent
Kishida et al. Interactions of poly (ethylene glycol)-grafted cellulose membranes with proteins and platelets
Mitzner et al. Extracorporeal endotoxin removal by immobilized polyethylenimine
US4276050A (en) Method for systemic endotoxin detection
US5801063A (en) Device and process for the biospecific removal of heparin
Breederveld et al. The localization of factor V within normal human platelets and the demonstration of a platelet‐factor V antigen in congenital factor V deficiency
Levin et al. Changes in platelet function during hemodialysis
GB2192633A (en) Endotoxin removal
Thompson et al. Removal of heparin and protamine from plasma
Cheung et al. Modulation of complement activation on hemodialysis membranes by immobilized heparin.
Parzer et al. Plasma protein adsorption to hemodialysis membranes: studies in an in vitro model
CA1283073C (en) Adsorbent for purification of blood coagulation factor viii and process for purification of blood coagulation factor viii using the same
Adamis et al. The proconvertin test: a simplified method and its application to the study of anticoagulant processes
Comfort et al. Immobilized enzyme cellulose hollow fibers: III. Physical properties and in vitro biocompatibility
US4180437A (en) Purification of antiserum for thrombosis test
Ostlund Jr Immunosorbent Chemistry: A Study of Agarose‐Based Column Sorbents for the Removal of Low‐Density Lipoprotein (LDL) from Blood
US5728437A (en) Articles exhibiting a blood-compatible surface layer and process for providing articles with such a surface layer

Legal Events

Date Code Title Description
WAP Application withdrawn, taken to be withdrawn or refused ** after publication under section 16(1)